WO2001084092A1 - Encapsulated float and method for making same - Google Patents
Encapsulated float and method for making same Download PDFInfo
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- WO2001084092A1 WO2001084092A1 PCT/US2001/013645 US0113645W WO0184092A1 WO 2001084092 A1 WO2001084092 A1 WO 2001084092A1 US 0113645 W US0113645 W US 0113645W WO 0184092 A1 WO0184092 A1 WO 0184092A1
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- WIPO (PCT)
- Prior art keywords
- float
- mixture
- accordance
- temperature
- hardness
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 23
- 229920001971 elastomer Polymers 0.000 claims abstract description 97
- 239000005060 rubber Substances 0.000 claims abstract description 97
- 239000000463 material Substances 0.000 claims abstract description 29
- 239000000126 substance Substances 0.000 claims abstract description 22
- 230000001681 protective effect Effects 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 11
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 77
- 239000000203 mixture Substances 0.000 claims description 66
- 229920003023 plastic Polymers 0.000 claims description 15
- 239000004033 plastic Substances 0.000 claims description 15
- -1 polyethylene Polymers 0.000 claims description 11
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 8
- 238000007906 compression Methods 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims description 8
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 239000004604 Blowing Agent Substances 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 229920000573 polyethylene Polymers 0.000 claims description 5
- 229920005989 resin Polymers 0.000 claims description 5
- 239000011347 resin Substances 0.000 claims description 5
- IANQTJSKSUMEQM-UHFFFAOYSA-N 1-benzofuran Chemical compound C1=CC=C2OC=CC2=C1 IANQTJSKSUMEQM-UHFFFAOYSA-N 0.000 claims description 4
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 4
- 235000021355 Stearic acid Nutrition 0.000 claims description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 229910052918 calcium silicate Inorganic materials 0.000 claims description 4
- 239000000378 calcium silicate Substances 0.000 claims description 4
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims description 4
- 239000006229 carbon black Substances 0.000 claims description 4
- 239000003822 epoxy resin Substances 0.000 claims description 4
- 125000000896 monocarboxylic acid group Chemical group 0.000 claims description 4
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 4
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 4
- 229920001568 phenolic resin Polymers 0.000 claims description 4
- 239000005011 phenolic resin Substances 0.000 claims description 4
- 229920000647 polyepoxide Polymers 0.000 claims description 4
- 239000008117 stearic acid Substances 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 239000011593 sulfur Substances 0.000 claims description 4
- KNXVOGGZOFOROK-UHFFFAOYSA-N trimagnesium;dioxido(oxo)silane;hydroxy-oxido-oxosilane Chemical compound [Mg+2].[Mg+2].[Mg+2].O[Si]([O-])=O.O[Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O KNXVOGGZOFOROK-UHFFFAOYSA-N 0.000 claims description 4
- 239000011787 zinc oxide Substances 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- AFZSMODLJJCVPP-UHFFFAOYSA-N dibenzothiazol-2-yl disulfide Chemical compound C1=CC=C2SC(SSC=3SC4=CC=CC=C4N=3)=NC2=C1 AFZSMODLJJCVPP-UHFFFAOYSA-N 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 3
- 229910052623 talc Inorganic materials 0.000 claims 3
- KPAPHODVWOVUJL-UHFFFAOYSA-N 1-benzofuran;1h-indene Chemical compound C1=CC=C2CC=CC2=C1.C1=CC=C2OC=CC2=C1 KPAPHODVWOVUJL-UHFFFAOYSA-N 0.000 claims 2
- 239000011253 protective coating Substances 0.000 claims 2
- 229920003051 synthetic elastomer Polymers 0.000 claims 1
- 239000005061 synthetic rubber Substances 0.000 claims 1
- 239000002253 acid Substances 0.000 abstract description 10
- 239000002904 solvent Substances 0.000 abstract description 9
- 150000007513 acids Chemical class 0.000 abstract description 8
- 229930195733 hydrocarbon Natural products 0.000 abstract description 8
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 8
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 75
- 238000012360 testing method Methods 0.000 description 42
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 31
- 238000010521 absorption reaction Methods 0.000 description 21
- 238000007654 immersion Methods 0.000 description 21
- 239000003502 gasoline Substances 0.000 description 17
- 238000005538 encapsulation Methods 0.000 description 14
- 239000011162 core material Substances 0.000 description 13
- 229920001169 thermoplastic Polymers 0.000 description 13
- 239000004416 thermosoftening plastic Substances 0.000 description 13
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 9
- 229920001821 foam rubber Polymers 0.000 description 8
- 229910017604 nitric acid Inorganic materials 0.000 description 8
- 239000002283 diesel fuel Substances 0.000 description 7
- 229910001220 stainless steel Inorganic materials 0.000 description 7
- 239000010935 stainless steel Substances 0.000 description 7
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 6
- 150000001298 alcohols Chemical class 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- MIMUSZHMZBJBPO-UHFFFAOYSA-N 6-methoxy-8-nitroquinoline Chemical compound N1=CC=CC2=CC(OC)=CC([N+]([O-])=O)=C21 MIMUSZHMZBJBPO-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000006261 foam material Substances 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 229920001903 high density polyethylene Polymers 0.000 description 4
- 239000004700 high-density polyethylene Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000036961 partial effect Effects 0.000 description 2
- YGSDEFSMJLZEOE-UHFFFAOYSA-N salicylic acid Chemical compound OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 240000001973 Ficus microcarpa Species 0.000 description 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 1
- 238000007551 Shore hardness test Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- WQPDQJCBHQPNCZ-UHFFFAOYSA-N cyclohexa-2,4-dien-1-one Chemical compound O=C1CC=CC=C1 WQPDQJCBHQPNCZ-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000010058 rubber compounding Methods 0.000 description 1
- 229960004889 salicylic acid Drugs 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 230000004584 weight gain Effects 0.000 description 1
- 235000019786 weight gain Nutrition 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F23/00—Indicating or measuring liquid level or level of fluent solid material, e.g. indicating in terms of volume or indicating by means of an alarm
- G01F23/30—Indicating or measuring liquid level or level of fluent solid material, e.g. indicating in terms of volume or indicating by means of an alarm by floats
- G01F23/76—Indicating or measuring liquid level or level of fluent solid material, e.g. indicating in terms of volume or indicating by means of an alarm by floats characterised by the construction of the float
Definitions
- This invention is in the field of rubber-based floats for measuring liquid levels.
- floats for liquid-level sensing in various applications, such as fuel tanks and liquid reservoirs, where the accurate and reliable measurement of the liquid level is important.
- Many floats are designed to include magnets, inserts, or guiding devices, all of which aid the float in performing its function.
- these guiding devices, inserts or magnets are molded within the float and actually become a part of a float assembly.
- Floats made of rubber materials are very popular because they are comparatively inexpensive, easy to manufacture into a variety of shapes and sizes and can be designed to meet a wide range of densities. Additionally, rubber-based floats are readily capable of being molded to include magnets, guiding devices, inserts, and the like, all of which aid the float in performing its function.
- Rubber-based floats have a tendency to fail or degrade in the presence of various chemicals, such as acids, certain hydrocarbons, chlorinated solvents, and alcohols. Failure or degradation of rubber-based floats in these environments is the result of either or both actual chemical attack of the rubber material or absorption of the chemical by the rubber-based float. Absorption can cause the float to fail by reason of an increase in weight or by fragmentation and/or cracking of the float.
- rubber-based floats are subject to partial or complete failure when utilized in conjunction with alcohols or products that are blended with alcohols.
- a non-alcohol compatible rubber-based float is used in conjunction with an alcohol or alcohol-blended product, the rubber material either absorbs or is attacked by the alcohol. Ultimately such absorption or attack will lead to the failure of the rubber-based float. Consequently, rubber-based floats have limited utility in these type chemical environments.
- rubber-based floats which: can be easily molded into various sizes and shapes; can be molded to accept internal magnets, sensors, guiding devices, inserts, and the like; are relatively easy and inexpensive to manufacture; have use within a wide range of applications; are resistant to attack or absorption from most chemicals, including most chlorinated solvents, hydrocarbons, alcohols, and acids; are safe from catastrophic failure; and effectively prevents float deterioration.
- a rubber float particularly of closed cell foam acrylonitrile rubber which is resistant to attack from, or absorption of, most chemicals, such as chlorinated solvents, acids, alcohols, and certain hydrocarbons.
- a float must be relatively inexpensive to manufacture, able to be molded into various sizes and shapes, and capable of being molded to include magnets, inserts, guiding devices, and the like.
- the float must also have an application within a wide range of temperatures and pressures.
- this invention comprises the encapsulation of acrylonitrile rubber-based float material within a container, such as polyethylene or some other thermoplastic, wherein the two are bonded together to create a closed-cell acrylonitrile rubber float, which is completely encapsulated within a precisely dimensional protective plastic skin.
- a float of this invention is virtually impervious to attack from or the absorption of most chemicals, while at the same time maintaining its low cost, broad application, and flexibility of design.
- the inventive float is also capable of being molded to include magnets, inserts, guiding devices, and the like.
- Fig. 1 including Figs. 1a and 1b, are transverse sectional views of two common prior art rubber floats;
- Fig. 2 including Figs. 2a and 2b, are transverse sectional views of two floats similar to those of Fig. 1 modified in accordance with this invention
- Fig. 3 is an enlarged fragmentary sectional view of the bond region between the acrylonitrile rubber core material and the thermoplastic protective skin;
- FIG. 4 including Figs. 4a and 4b, 4a is a perspective view of a cylindrical float just prior to the encapsulation step, and Fig. 4b is a cross section of the float of Fig. 4a;
- Fig. 5 is a flow diagram for step 1 , stage 1 of the process of this invention.
- Fig. 6 is a flow diagram for step 1 , stage 2 of the process of this invention.
- Fig. 7 is a flow diagram of step 1 , stage 3 of the process of this invention.
- Fig. 8 is a flow diagram of step 2 the encapsulation.
- Acrylonitrile rubber floats have been used for years for liquid level sensing; however, their use has been limited to those situations where the environment in which the float was utilized did not also include chemicals, which would either attack or be absorbed by the acrylonitrile rubber. Such attack or absorption could eventually result in the partial or complete failure of the float, and possibly culminate in human tragedy.
- the present invention is concerned with rubber-based floats, particularly an acrylonitrile rubber float, which is encapsulated in a protective skin, and method for making same.
- the skin protects the float from attack by various chemicals, which are aggressive towards and degrade acrylonitrile rubber, e.g., chlorinated solvents, acids, and certain hydrocarbons.
- the skin acts to eliminate absorption by the acrylonitrile rubber of various chemicals, such as alcohols, chlorinated solvents, acids, and certain hydrocarbons.
- the encapsulated acrylonitrile rubber float of this invention is manufactured in basically a two-step process.
- the first step is the manufacture of the acrylonitrile rubber float material or preform, with the second step being the encapsulation of the acrylonitrile rubber float material within a protective skin. Encapsulation does not alter the float's functionality or performance; however, it does allow the float to resist attack by or absorption of most other chemicals.
- Fig. 1 is comprised of Figs. 1a and 1b, both of which depict two types of commercially available prior art acrylonitrile rubber floats, neither of which is encapsulated.
- the floats of Fig. 1 are both comprised of acrylonitrile rubber material A.
- Fig. 1a reveals an insert I
- Fig. 1 b reveals a carburetor pivot arm PA, both of which are imbedded within and held in place by the acrylonitrile rubber material.
- Fig. 2 comprised of Figs. 2a and 2b, illustrates an encapsulated version of the same type floats of Fig. 1.
- Fig. 2 depicts the protective skin 11 , which encapsulates and protects the entire float.
- the protective skin does not alter the float's appearance or volume nor does it alter the float's functionality. This protective skin does eliminate all of the problems associated with the embodiment of Figs. 1a and 1 b as disclosed above.
- Fig. 2b reveals an insert 12 within acrylonitrile rubber material 13, while Fig. 2a shows an encapsulated float with a carburetor pivot arm insert 14 within the acrylonitrile rubber material.
- Fig. 3 illustrates a closed cell acrylonitrile rubber core material 13 in bonding engagement 20 with the protective plastic skin 11.
- Thermoplastics such as high and low-density polyethylene or high and low-density polypropylene may be used to encapsulate the acrylonitrile rubber float material 13.
- the acrylonitrile rubber core material 13 and the thermoplastic 11 form a strong bond at their interface 20.
- the bond is sufficiently strong to withstand attempts to separate the core material from the skin, and may be mechanical, thermal or chemical.
- thermoplastic skin 11 Attempts to separate the thermoplastic skin 11 from the acrylonitrile rubber core material 13 by hand have been unsuccessful.
- the encapsulated float of this invention will actually tear before the bond 20 between the thermoplastic skin 11 and acrylonitrile rubber core 13 will break.
- the bond 20 between the acrylonitrile rubber core material 13 and the thermoplastic skin 11 results in a unitary float body.
- the skin 11 is approximately 0.02 to 0.06 of an inch thick; however, wall thickness can be designed to meet the demands of the environment.
- the skin also produces a precise weight change factor, which is designed into the float.
- Fig. 4a illustrates a cylindrical float just before the encapsulation step, wherein the acrylonitrile rubber core material 13 is placed into the preformed skin 11c with lid 11 L.
- Fig. 4b illustrates a cross section of Fig. 4a just prior to the bonding of the acrylonitrile rubber core material 13 to the protective skin 11 (11c and 11 L).
- the significance of the inventive float is that the acrylonitrile rubber core material 13 enters into complete bonding engagement at the interface 20 of the thermoplastic skin 11 , providing uniform protection of the core material 13 from the outside chemical environment.
- Step one is comprised of three separate stages:
- the first stage, or Banbury mix, Fig. 5, occurs as follows: Blending in a Banbury Mill or the like, by weight, add between 30.0% to 55.0% (37.04% to 37.50%) acrylonitrile rubber, 0.5% to 4.2% (0.84% to 1.01 %) zinc oxide, 1.0% to 15.0% (1.67% to 2.02%) stearic acid, 0.1% to 2.0% (0.21 to 0.51 %) retarder SAX salicylic acid (0-hydroxybenzoic acid) C 6 H 4 (0H)(COOH), 3.0% to 22.0% (14.14% to 15.83%) mistron vapor Mg 3 Si4010 (OH) 2 , 0.3% to 2.75% (0.83% to 1.35%) Coumarone lndene Resin absorbed on Synthetic Calcium Silicate (72% Cumar P- 25), and 8.0% to 15.0% (10.10% to 10.83%) sulfur, while maintaining the temperature of the mixture to below 250°F.
- the inventor has determined that, for best results, the addition of the compounds in the Banbury stage should occur in the sequence set forth above.
- Blending is completed after a period of 60 to 180 minutes or when the mixture turns a pale yellow-brown in color.
- the Shore A hardness of the mixture is between 15-90.
- the Shore A hardness is between 65 and 75.
- stage one mixture Transfer the completed stage one mixture to a suitably sized roller mill to begin stage 2, as shown in Fig. 6.
- stage one mixture add by weight, between 12.0% to 40.0% (22.22% to 22.50%) phenolic resin (C 6 H 6 O.CH 2 O)X, 2.5% to 10.0% (3.33% to 4.03%) carbon black, 0.25% to 1.5% (0.63% to 0.84%) Altax C 14 H 8 N 2 S 4 , 1.75% to 15% (2.50% to 2.70%) epoxy-resin, and finally 1.0% to 5.0% (3.33% to 4.04%) blowing agent (NO) 2 C5H 10 N 4 , while controlling the temperature of the mixture throughout this stage to less than 200°F.
- the inventor has determined that for best results, the addition of compounds in roller mix stage should also occur in the sequence listed above.
- Mixing is completed in approximately 15 to 50 minutes or when the mixture is uniform and turns to a black, smooth sheet.
- Shore A hardness test is conducted to confirm hardness of between 15 and 90.
- the Shore A hardness is between 65 and 75.
- the compression stage of Fig. 6 is the third and final stage of step 1.
- the pre-cured acrylonitrile rubber-based mixture of completed step 2 is placed into a conventional compression tool where, depending upon the formation, the pressure is increased to between 20-900 lbs/cubic inch for between 5 to 45 minutes at a temperature of between 200°F. to 350°F., Fig. 7.
- the pressure in this stage is between 350 and 410 lbs/cubic inch for 10 to 18 minutes at a temperature of between 265°F. and 275°F.
- the acrylonitrile rubber foam is removed from the compression tool and allowed to cool. Cooling may be achieved in air or by any convention manner.
- the acrylonitrile rubber foam After the acrylonitrile rubber foam has cooled, it is inspected for visual defects in preparation for the encapsulation step. The foam material is tested again to confirm that its Shore A hardness is between 15-90. For the preferred embodiment, the Shore A hardness is between 65 and 75.
- any magnets, inserts, guides, or the like are placed into the acrylonitrile rubber foam by conventional means, such as drilling an opening and inserting the inset in place.
- Thermoplastic containers which have been pre-molded to meet the desired size and shape specifications, are visually inspected for defects.
- the inventor has determined that both high and low-density polyethylene, and high and low-density polypropylene, bond equally as well with the acrylonitrile rubber core material.
- the pre-molded thermoplastic is in a container shape and is preferably formed to have only one open end or lid and thus only one seam, although multi-seam containers may be used.
- the inventor has determined that the physical characteristics of the encapsulation material, e.g., wall thickness, is more easily controlled when it is premolded. By contrast, dipping, painting or spraying the acrylonitrile rubber foam material with the encapsulation material would likely result in a non-uniform skin, and thus an improper float.
- the physical characteristics of the encapsulation material e.g., wall thickness
- the desired weight of pre-cured acrylonitrile rubber foam unit taking into account the container and lid weight, is placed into the thermoplastic container, to fill the space.
- the container lid is loosely placed onto the container, to close the container and meet final products dimensional requirements.
- the plastic container, with acrylonitrile rubber core material and/or insert are placed into a finish mold tool.
- the finish mold tool is designed to conform to the size and shape of the thermoplastic container.
- the inventor has, for purposes of this application, elected to describe the encapsulation process wherein high-density polyethylene is utilized as the encapsulation material.
- the finish mold tool is, depending on formulation, heated by any conventional means to between 250°F. to 550°F. for between 20 to 180 minutes to allow the acrylonitrile rubber material to expand into intimate contact with the entire interior surface of the thermoplastic container and enter into bonding engagement thereto. During this step, the container and lid are also bonded to seal the float .
- the finish mold tool is heated to between 250°F. to 500°F. for between 30 to 70 minutes.
- the temperature and time may vary where high-density polyethylene, or high and low-density polypropylene, are used as the encapsulation material.
- the finished mold tool is allowed to cool by any conventional means until it is ambient temperature.
- the acrylonitrile rubber foam material with insert, if any, is bonded to and encapsulated within the protective polyethylene skin, Figs. 2 and 3.
- the resultant float is now a unitary body.
- Table 1 is a summary of results of a Shore A hardness test comparing the acrylonitrile rubber encapsulated float of the invention (denoted U-2000) with two non-encapsulated, but commercially available acrylonitrile rubber floats denoted "A" and "B” after a methanol soak. The three floats were submerged in a 100% methanol bath and allowed to soak for 28 days at a temperature of between about 64° to 78°F.
- the acrylonitrile rubber float of this invention did not lose any of its Shore A hardness, while the two competitive but non-encapsulated acrylonitrile rubber floats lost 17.5 points of hardness (A float) and 11.5 points of hardness (B float), respectively.
- Table 2 presents the results of a methanol immersion test comparing the same three types of floats, as utilized in Table 1.
- the three floats were again immersed into a 100% methanol bath for 28 days. This test measured the amount of methanol absorbed by each float as an increase in each float's weight. Each day the floats were removed from the methanol bath, weighed and returned to the methanol bath.
- the encapsulated acrylonitrile rubber float of this invention exhibited only 0.01 grams weight gain after 28 days, while the two non-encapsulated, acrylonitrile rubber floats exhibited a significantly higher increase in weight.
- Acrylonitrile rubber float A increased 8.20 grams in weight after 28 days, while the B acrylonitrile rubber float increased 9.62 grams in weight after 28 days.
- Applicant wishes to point out that in regards to Tables 2-7, applicant was required to remove excess liquid from the floats by hand blotting prior to weighing. Hand blotting was used for measurement purposes during testing and did not result in completely dry samples.
- Table 3 sets forth the results of the 1 ,1 ,1 Trichloroethane immersion test.
- the same three types of floats, as described in Table 1 were immersed in 100% 1 ,1 ,1 trichloroethane at a temperature of between 150°F. to 170°F.
- the test measured the amount of 1 ,1 ,1 trichloroethane absorbed by each float as an increase in each float's weight. Each day the floats were removed from the bath and weighted then returned to the bath.
- the acrylonitrile rubber float of this invention (U-2000) increased only 0.02 grams in weight over a 24-hour period, while acrylonitrile rubber float A increased 30.83 grams in weight after only one hour, and acrylonitrile rubber float B increased 29.32 grams weight after only one hour. Both the A and the B floats were partially dissolved, severely swollen, and severely cracked after only one hour of immersion in the 1 ,1 ,1 trichloroethane. The conclusion from this test is that a non-encapsulated float would fail in a short period of time in this chlorinated solvent, whereas the inventive float would not.
- Table 4 sets forth the results of an immersion test in an alcohol/gasoline blend, whereby two commercially available acrylonitrile rubber-based floats, A and C as well as the encapsulated acrylonitrile rubber float (U-2000) of this invention were immersed in a blend of 15% methanol and 85% regular unleaded commercially available gasoline by weight.
- the immersion test was conducted over 28 days at a temperature of between 68° to 77°F.
- the test measured the amount of absorption of the methanol/gasoline blend by each float as an increase in weight of each float. Each day the floats were removed from the bath, weighed and then returned to the bath.
- the encapsulated acrylonitrile rubber float increased 0.01 grams in weight after 28 days, while acrylonitrile rubber float A increased 0.8 grams in weight, and acrylonitrile rubber float C increased 0.9 grams in weight.
- Table 5 describes the results of an ethanol immersion test wherein the same three types of floats as described in Table 4 were submerged in 100% ethanol for 28 days.
- the temperature during the 28-day test was between 64° and 78°F.
- the test measured the amount of ethanol absorbed by each float as an increase in weight of each float. Each day the floats were removed from the bath, weighed and returned to the bath.
- Both the A acrylonitrile rubber float and the C acrylonitrile rubber float increased 0.2 grams in weight, while the encapsulated acrylonitrile rubber float of this invention increased only 0.01 grams in weight.
- Table 6 summarizes the results of a float immersion test in a 15% ethanol and 85% commercially available Regular Unleaded gasoline blend.
- the test measured the absorption of the ethanol gasoline blend by each float as an increase in the weight of each float over a 28-day period. This test was conducted at temperatures ranging from 64° to 78°F. The same three types of floats, as disclosed in Table 4, were utilized. Each day the floats were removed from the bath, weighed and returned to the bath.
- the A non-encapsulated acrylonitrile rubber float increased 0.5 grams and the C non-encapsulated acrylonitrile rubber float increased 0.6 grams in 28 days, while the encapsulated acrylonitrile rubber float of this invention (U-2000) only increased 0.01 grams during the same time period.
- Table 7 sets forth the results of the diesel fuel immersion test.
- the test was conducted at temperatures of between 64° and 78°F. for 28 days and measured the amount of diesel fuel absorbed as an increase in weight of each float. Each day the floats were removed from the bath, weighed and returned to the bath. Both the A and C acrylonitrile rubber floats increased 0.7 grams in weight while the encapsulated acrylonitrile rubber float of this invention increased 0.07 grams in weight during the 28-day test.
- Table 8 sets forth the affects of a nitric acid and ammonium bifluoride mixture on encapsulated and non-encapsulated acrylonitrile rubber floats.
- Four separate floats were introduced into a nitric acid mixture comprised of 250 ml of 70% commercial grade nitric acid and 27 grams ammonium bifluoride.
- Two of the floats were commercially available non-encapsulated acrylonitrile rubber floats, denoted A and C.
- the other remaining floats were the encapsulated acrylonitrile rubber float of this invention, and a commercially available hollow, stainless steel float.
- Each float was allowed to float upon the nitric acid mixture, thus directly exposing the bottom and portions of the side of each float to the acid mixture.
- Table 1 is a summary of results for Shore A hardness after a methanol soak
- Table 2 is a summary of absorption after a methanol immersion
- Table 3 is a summary of absorption after a 1 ,1 ,1 trichloroethane immersion
- Table 4 is a summary of absorption results after immersion in a 15% methanol, 85% regular unleaded gasoline mixture
- Table 5 is a summary of absorption results after an ethanol immersion
- Table 6 is a summary of absorption results after immersion in a 15% ethanol, 85% regular unleaded gasoline mixture
- Table 7 is a summary of absorption results after a diesel fuel immersion.
- Table 8 is a summary of float degradation after a nitric acid/ammonium bifluoride mixture soak.
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Abstract
A float, including rubber material (13), for sensing liquid levels having a chemically resistant protective covering (11), said float having greater resistance to attack from chemicals, such as hydrocarbons, acids, and chlorinated solvents, said float may be made to include magnets, guiding devices or sensors.
Description
ENCAPSULATED FLOAT AND METHOD FOR MAKING SAME
REFERENCE TO RELATED APPLICATION
This application claims benefit of U.S. Provisional Patent Application Serial No. 60/201.022 filed May 1 , 2000, and hereby claims the benefit of the embodiments therein and of the filing date thereof.
FIELD OF THE INVENTION
This invention is in the field of rubber-based floats for measuring liquid levels.
BACKGROUND OF THE INVENTION
Virtually every industry utilizes floats for liquid-level sensing in various applications, such as fuel tanks and liquid reservoirs, where the accurate and reliable measurement of the liquid level is important. Many floats are designed to include magnets, inserts, or guiding devices, all of which aid the float in performing its function. Generally, these guiding devices, inserts or magnets are molded within the float and actually become a part of a float assembly.
Floats made of rubber materials, such as acrylonitrile rubber, are very popular because they are comparatively inexpensive, easy to manufacture into a variety of shapes and sizes and can be designed to meet a wide range of densities.
Additionally, rubber-based floats are readily capable of being molded to include magnets, guiding devices, inserts, and the like, all of which aid the float in performing its function.
In spite of the aforementioned benefits of rubber-based floats, there is one significant disadvantage to their use. Rubber-based floats have a tendency to fail or degrade in the presence of various chemicals, such as acids, certain hydrocarbons, chlorinated solvents, and alcohols. Failure or degradation of rubber-based floats in these environments is the result of either or both actual chemical attack of the rubber material or absorption of the chemical by the rubber-based float. Absorption can cause the float to fail by reason of an increase in weight or by fragmentation and/or cracking of the float.
Today, many Federal, State and Municipal governments have offered financial incentives to individuals, businesses, and governmental agencies that utilize a fuel which is less polluting. One type of fuel which has gained popularity is an alcohol-gasoline blend. It has been found that use of such blends may lower a vehicle's emissions. With this key benefit in mind, many fuel manufacturers have spent considerable sums of money in developing and improving the alcohol-gasoline blends and have added alcohol-blended fuels to their product line.
As mentioned earlier, rubber-based floats are subject to partial or complete failure when utilized in conjunction with alcohols or products that are blended with alcohols. In cases where a non-alcohol compatible rubber-based float is used in conjunction with an alcohol or alcohol-blended product, the rubber material either absorbs or is attacked by the alcohol. Ultimately such absorption or attack will lead
to the failure of the rubber-based float. Consequently, rubber-based floats have limited utility in these type chemical environments.
Exposure to other chemicals, such as chlorinated solvents, acids, and certain hydrocarbons, may also lead to the failure of a rubber-based float. Failure under these circumstances also occurs by attack or degradation of the float by the chemicals or by absorption by the rubber material of the chemical. Again, the inadvertent introduction of an incompatible float into a fuel tank or reservoir containing chlorinated solvents, certain hydrocarbons, or acids could lead to the failure of the rubber-based float, which in turn could result in serious, catastrophic, or possibly tragic consequences.
To date, the only means known to overcome the chemical incompatibility problems of rubber-based floats was to simply avoid their use in certain chemical environments.
As a result of the aforementioned problems in using rubber-based floats, it is the object of this invention to develop rubber-based floats which: can be easily molded into various sizes and shapes; can be molded to accept internal magnets, sensors, guiding devices, inserts, and the like; are relatively easy and inexpensive to manufacture; have use within a wide range of applications; are resistant to attack or absorption from most chemicals, including most chlorinated solvents, hydrocarbons, alcohols, and acids; are safe from catastrophic failure; and
effectively prevents float deterioration.
BRIEF DESCRIPTION OF THE INVENTION
In light of the state of the art, the inventor has set out to produce a rubber float, particularly of closed cell foam acrylonitrile rubber which is resistant to attack from, or absorption of, most chemicals, such as chlorinated solvents, acids, alcohols, and certain hydrocarbons. Such a float must be relatively inexpensive to manufacture, able to be molded into various sizes and shapes, and capable of being molded to include magnets, inserts, guiding devices, and the like. The float must also have an application within a wide range of temperatures and pressures.
These objects, and others, which will become apparent upon consideration of the following disclosure, are achieved by this invention, which briefly stated comprises the encapsulation of acrylonitrile rubber-based float material within a container, such as polyethylene or some other thermoplastic, wherein the two are bonded together to create a closed-cell acrylonitrile rubber float, which is completely encapsulated within a precisely dimensional protective plastic skin. A float of this invention is virtually impervious to attack from or the absorption of most chemicals, while at the same time maintaining its low cost, broad application, and flexibility of design. The inventive float is also capable of being molded to include magnets, inserts, guiding devices, and the like.
BRIEF DESCRIPTION OF THE DRAWINGS
This invention may be more clearly understood with the following detailed description and by reference to the drawings in which:
Fig. 1 , including Figs. 1a and 1b, are transverse sectional views of two common prior art rubber floats;
Fig. 2, including Figs. 2a and 2b, are transverse sectional views of two floats similar to those of Fig. 1 modified in accordance with this invention;
Fig. 3 is an enlarged fragmentary sectional view of the bond region between the acrylonitrile rubber core material and the thermoplastic protective skin;
Fig. 4, including Figs. 4a and 4b, 4a is a perspective view of a cylindrical float just prior to the encapsulation step, and Fig. 4b is a cross section of the float of Fig. 4a;
Fig. 5 is a flow diagram for step 1 , stage 1 of the process of this invention;
Fig. 6 is a flow diagram for step 1 , stage 2 of the process of this invention;
Fig. 7 is a flow diagram of step 1 , stage 3 of the process of this invention; and
Fig. 8 is a flow diagram of step 2 the encapsulation.
DETAILED DESCRIPTION OF THE INVENTION
Acrylonitrile rubber floats have been used for years for liquid level sensing; however, their use has been limited to those situations where the environment in which the float was utilized did not also include chemicals, which would either attack or be absorbed by the acrylonitrile rubber. Such attack or absorption could eventually result in the partial or complete failure of the float, and possibly culminate in human tragedy.
The present invention is concerned with rubber-based floats, particularly an acrylonitrile rubber float, which is encapsulated in a protective skin, and method for making same. The skin protects the float from attack by various chemicals, which are aggressive towards and degrade acrylonitrile rubber, e.g., chlorinated solvents, acids, and certain hydrocarbons. In still other cases, the skin acts to eliminate absorption by the acrylonitrile rubber of various chemicals, such as alcohols, chlorinated solvents, acids, and certain hydrocarbons.
The encapsulated acrylonitrile rubber float of this invention is manufactured in basically a two-step process. The first step is the manufacture of the acrylonitrile rubber float material or preform, with the second step being the encapsulation of the acrylonitrile rubber float material within a protective skin. Encapsulation does not alter the float's functionality or performance; however, it does allow the float to resist attack by or absorption of most other chemicals.
THE PRODUCT
Fig. 1 is comprised of Figs. 1a and 1b, both of which depict two types of commercially available prior art acrylonitrile rubber floats, neither of which is encapsulated. The floats of Fig. 1 are both comprised of acrylonitrile rubber material A. Fig. 1a reveals an insert I, and Fig. 1 b reveals a carburetor pivot arm PA, both of which are imbedded within and held in place by the acrylonitrile rubber material.
The above-mentioned inserts aid the float in performing its function. Floats, such as these, are subject to attack by or absorption of various chemicals, as shown later in Tables 1-8, resulting in change in weight, volume or durability of the float.
Fig. 2, comprised of Figs. 2a and 2b, illustrates an encapsulated version of the same type floats of Fig. 1. Fig. 2 depicts the protective skin 11 , which encapsulates and protects the entire float. The protective skin does not alter the float's appearance or volume nor does it alter the float's functionality. This protective skin does eliminate all of the problems associated with the embodiment of Figs. 1a and 1 b as disclosed above.
Fig. 2b reveals an insert 12 within acrylonitrile rubber material 13, while Fig. 2a shows an encapsulated float with a carburetor pivot arm insert 14 within the acrylonitrile rubber material.
A comparison of the floats of Fig. 1 with those of Fig. 2 reveals that the encapsulated floats are virtually identical to the non-encapsulated floats in both size, shape and weight, except that the encapsulated floats are more resistant to chemical attack or absorption, then a non-encapsulated float. A comparison of the performance of the non-encapsulated float and encapsulated floats is set forth in
detail in Tables 1-8 below.
Turning now to Fig. 3, which illustrates a closed cell acrylonitrile rubber core material 13 in bonding engagement 20 with the protective plastic skin 11. Thermoplastics, such as high and low-density polyethylene or high and low-density polypropylene may be used to encapsulate the acrylonitrile rubber float material 13.
As can be seen in Fig. 3, the acrylonitrile rubber core material 13 and the thermoplastic 11 form a strong bond at their interface 20. The bond is sufficiently strong to withstand attempts to separate the core material from the skin, and may be mechanical, thermal or chemical.
Attempts to separate the thermoplastic skin 11 from the acrylonitrile rubber core material 13 by hand have been unsuccessful. The encapsulated float of this invention will actually tear before the bond 20 between the thermoplastic skin 11 and acrylonitrile rubber core 13 will break. The bond 20 between the acrylonitrile rubber core material 13 and the thermoplastic skin 11 results in a unitary float body.
The skin 11 is approximately 0.02 to 0.06 of an inch thick; however, wall thickness can be designed to meet the demands of the environment. The skin also produces a precise weight change factor, which is designed into the float.
Fig. 4a illustrates a cylindrical float just before the encapsulation step, wherein the acrylonitrile rubber core material 13 is placed into the preformed skin 11c with lid 11 L. Fig. 4b illustrates a cross section of Fig. 4a just prior to the bonding of the acrylonitrile rubber core material 13 to the protective skin 11 (11c and 11 L).
The significance of the inventive float is that the acrylonitrile rubber core material 13 enters into complete bonding engagement at the interface 20 of the
thermoplastic skin 11 , providing uniform protection of the core material 13 from the outside chemical environment.
THE PROCESS
Turning now to step one, as shown in Figs. 5, 6, 7, and 8 of the manufacture of the acrylonitrile rubber-based float material. Step one is comprised of three separate stages:
Stage 1 , the Banbury mix Stage 2, the roller mix Stage 3, the compression stage. In both the Banbury stage, Fig. 5, and the roller mill stage, Fig. 6, below, the inventor has set forth a wide range of the additives to be mixed. This represents the broad range of acrylonitrile rubber formulations presently utilized within the industry. The exact formulation will vary with the consumer needs and specifications.
The preferred embodiment, which is the most common of these formulations, is set forth in parenthesis beside each ingredient additive range.
I
The first stage, or Banbury mix, Fig. 5, occurs as follows: Blending in a Banbury Mill or the like, by weight, add between 30.0% to 55.0% (37.04% to 37.50%) acrylonitrile rubber, 0.5% to 4.2% (0.84% to 1.01 %) zinc oxide, 1.0% to 15.0% (1.67% to 2.02%) stearic acid, 0.1% to 2.0% (0.21 to 0.51 %) retarder SAX salicylic acid (0-hydroxybenzoic acid) C6H4 (0H)(COOH), 3.0% to 22.0% (14.14% to
15.83%) mistron vapor Mg3Si4010 (OH)2, 0.3% to 2.75% (0.83% to 1.35%) Coumarone lndene Resin absorbed on Synthetic Calcium Silicate (72% Cumar P- 25), and 8.0% to 15.0% (10.10% to 10.83%) sulfur, while maintaining the temperature of the mixture to below 250°F.
The inventor has determined that, for best results, the addition of the compounds in the Banbury stage should occur in the sequence set forth above.
Blending is completed after a period of 60 to 180 minutes or when the mixture turns a pale yellow-brown in color.
Upon completion of the Banbury mixture stage, confirm that the Shore A hardness of the mixture is between 15-90. For the preferred embodiment, the Shore A hardness is between 65 and 75.
II
Transfer the completed stage one mixture to a suitably sized roller mill to begin stage 2, as shown in Fig. 6. To the stage one mixture, add by weight, between 12.0% to 40.0% (22.22% to 22.50%) phenolic resin (C6H6O.CH2O)X, 2.5% to 10.0% (3.33% to 4.03%) carbon black, 0.25% to 1.5% (0.63% to 0.84%) Altax C14H8N2S4, 1.75% to 15% (2.50% to 2.70%) epoxy-resin, and finally 1.0% to 5.0% (3.33% to 4.04%) blowing agent (NO)2C5H10N4, while controlling the temperature of the mixture throughout this stage to less than 200°F. The inventor has determined that for best results, the addition of compounds in roller mix stage should also occur in the sequence listed above.
Mixing is completed in approximately 15 to 50 minutes or when the mixture is
uniform and turns to a black, smooth sheet.
A Shore A hardness test is conducted to confirm hardness of between 15 and 90. For the preferred embodiment, the Shore A hardness is between 65 and 75.
The compression stage of Fig. 6 is the third and final stage of step 1. The pre-cured acrylonitrile rubber-based mixture of completed step 2 is placed into a conventional compression tool where, depending upon the formation, the pressure is increased to between 20-900 lbs/cubic inch for between 5 to 45 minutes at a temperature of between 200°F. to 350°F., Fig. 7. In the preferred embodiment, the pressure in this stage is between 350 and 410 lbs/cubic inch for 10 to 18 minutes at a temperature of between 265°F. and 275°F.
The acrylonitrile rubber foam is removed from the compression tool and allowed to cool. Cooling may be achieved in air or by any convention manner.
After the acrylonitrile rubber foam has cooled, it is inspected for visual defects in preparation for the encapsulation step. The foam material is tested again to confirm that its Shore A hardness is between 15-90. For the preferred embodiment, the Shore A hardness is between 65 and 75.
The acrylonitrile rubber foam material is weighed and trimmed of any excess material, if necessary, to meet the desired unit shape and weight. Stage Three and Step One are now complete.
IV
The acrylonitrile rubber foam is now ready for the encapsulation step Fig. 8. However, prior to the encapsulation step, any magnets, inserts, guides, or the like are placed into the acrylonitrile rubber foam by conventional means, such as drilling an opening and inserting the inset in place.
Thermoplastic containers, which have been pre-molded to meet the desired size and shape specifications, are visually inspected for defects. The inventor has determined that both high and low-density polyethylene, and high and low-density polypropylene, bond equally as well with the acrylonitrile rubber core material. The pre-molded thermoplastic is in a container shape and is preferably formed to have only one open end or lid and thus only one seam, although multi-seam containers may be used.
The inventor has determined that the physical characteristics of the encapsulation material, e.g., wall thickness, is more easily controlled when it is premolded. By contrast, dipping, painting or spraying the acrylonitrile rubber foam material with the encapsulation material would likely result in a non-uniform skin, and thus an improper float.
The desired weight of pre-cured acrylonitrile rubber foam unit, taking into account the container and lid weight, is placed into the thermoplastic container, to fill the space. The container lid is loosely placed onto the container, to close the container and meet final products dimensional requirements. Thereafter, the plastic container, with acrylonitrile rubber core material and/or insert, are placed into a finish mold tool. The finish mold tool is designed to conform to the size and shape of the
thermoplastic container. The inventor has, for purposes of this application, elected to describe the encapsulation process wherein high-density polyethylene is utilized as the encapsulation material.
Thereafter, the finish mold tool is, depending on formulation, heated by any conventional means to between 250°F. to 550°F. for between 20 to 180 minutes to allow the acrylonitrile rubber material to expand into intimate contact with the entire interior surface of the thermoplastic container and enter into bonding engagement thereto. During this step, the container and lid are also bonded to seal the float .
For the preferred embodiment, the finish mold tool is heated to between 250°F. to 500°F. for between 30 to 70 minutes. The temperature and time may vary where high-density polyethylene, or high and low-density polypropylene, are used as the encapsulation material. After the allotted time period, the finished mold tool is allowed to cool by any conventional means until it is ambient temperature. Upon completion of this step, the acrylonitrile rubber foam material with insert, if any, is bonded to and encapsulated within the protective polyethylene skin, Figs. 2 and 3. The resultant float is now a unitary body.
In the description of the process above, the temperatures, times and quantities have been shown to be successful in manufacturing said float; however, it is believed that minor variations in time, temperature and quantity would also yield an acceptable product.
Table 1 is a summary of results of a Shore A hardness test comparing the acrylonitrile rubber encapsulated float of the invention (denoted U-2000) with two non-encapsulated, but commercially available acrylonitrile rubber floats denoted "A"
and "B" after a methanol soak. The three floats were submerged in a 100% methanol bath and allowed to soak for 28 days at a temperature of between about 64° to 78°F.
After removal from the methanol soak each day, the floats were each given identical shore hardness tests and then returned to the bath.
As shown in Table 1 , the acrylonitrile rubber float of this invention did not lose any of its Shore A hardness, while the two competitive but non-encapsulated acrylonitrile rubber floats lost 17.5 points of hardness (A float) and 11.5 points of hardness (B float), respectively.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb any methanol and thus lose hardness, as compared with non-encapsulated floats.
TABLE 1
Methanol Soak - Shore A Hardness Test Parameter - Temperature 64-78 Deg. F, Commercial Grade Methanol (CAS 67-56-1 )
A B U-2000
Start 94.5 95.5 93
Day 1 92 94.5 93
Day 2 89 93 93
Day 3 87 93 93
Day 4 87 92 93
Day 8 86 92 93
Day 9 86 90 93
Day 10 85 90 93
Day 14 82 87 93
Day 17 80 87 93
Day 22 78 85 93
Day 28 77 84 93
Turning now to Table 2, which presents the results of a methanol immersion test comparing the same three types of floats, as utilized in Table 1. Here, the three floats were again immersed into a 100% methanol bath for 28 days. This test measured the amount of methanol absorbed by each float as an increase in each float's weight. Each day the floats were removed from the methanol bath, weighed and returned to the methanol bath.
The encapsulated acrylonitrile rubber float of this invention exhibited only 0.01 grams weight gain after 28 days, while the two non-encapsulated, acrylonitrile rubber floats exhibited a significantly higher increase in weight. Acrylonitrile rubber float A increased 8.20 grams in weight after 28 days, while the B acrylonitrile rubber float increased 9.62 grams in weight after 28 days.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb significant amounts of methanol over the test period, whereas non-encapsulated floats did absorb a substantial amount of methanol.
Applicant wishes to point out that in regards to Tables 2-7, applicant was required to remove excess liquid from the floats by hand blotting prior to weighing. Hand blotting was used for measurement purposes during testing and did not result in completely dry samples.
TABLE 2
Methanol Immersion Weight Change (gms) Testing
Temperature 64-78 Deg. F
Commercial Grade Methanol (CAS 67-56-1 )
A B U-2000
Start 48.48 53.96 8.02
Day 1 49.03 54.33 8.03
Day 2 49.55 54.83 8.02
Day 3 49.88 55.43 8.02
Day 4 50.20 55.96 8.08
Day 8 51.02 57.58 8.08
Day 9 51.60 57.85 8.09
Day 10 51.86 58.10 8.05
Day 11 51.93 58.36 8.04
Day 14 52.81 59.28 8.03
Day 17 53.73 60.08 8.06
Day 22 55.09 61.41 8.04
Day 28 56.28 62.58 8.03
Referring now to Table 3, which sets forth the results of the 1 ,1 ,1 Trichloroethane immersion test. The same three types of floats, as described in Table 1 , were immersed in 100% 1 ,1 ,1 trichloroethane at a temperature of between 150°F. to 170°F. The test measured the amount of 1 ,1 ,1 trichloroethane absorbed by each float as an increase in each float's weight. Each day the floats were removed from the bath and weighted then returned to the bath.
The acrylonitrile rubber float of this invention (U-2000) increased only 0.02 grams in weight over a 24-hour period, while acrylonitrile rubber float A increased 30.83 grams in weight after only one hour, and acrylonitrile rubber float B increased
29.32 grams weight after only one hour. Both the A and the B floats were partially dissolved, severely swollen, and severely cracked after only one hour of immersion in the 1 ,1 ,1 trichloroethane. The conclusion from this test is that a non-encapsulated float would fail in a short period of time in this chlorinated solvent, whereas the inventive float would not.
TABLE 3
1 ,1 ,1 , Trichloroethane Absorption Immersion Test (gms) - Hot
A B U-2000
Start 48.22 54.05 8.17
Hour 1 79.05 3.37 8.21
Hour 8 * * 8.2
Hour 24 * * 8.19
*- Sample failure after 1 hour - sample partially dissolved, severely cracked, severely swollen.
Table 4 sets forth the results of an immersion test in an alcohol/gasoline blend, whereby two commercially available acrylonitrile rubber-based floats, A and C as well as the encapsulated acrylonitrile rubber float (U-2000) of this invention were immersed in a blend of 15% methanol and 85% regular unleaded commercially available gasoline by weight. The immersion test was conducted over 28 days at a temperature of between 68° to 77°F. The test measured the amount of absorption of the methanol/gasoline blend by each float as an increase in weight of each float. Each day the floats were removed from the bath, weighed and then returned to the bath.
The encapsulated acrylonitrile rubber float increased 0.01 grams in weight
after 28 days, while acrylonitrile rubber float A increased 0.8 grams in weight, and acrylonitrile rubber float C increased 0.9 grams in weight.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb significant amounts of the methanol/gasoline mixture over the test period, whereas non-encapsulated floats did absorb a substantial amount of the methanol/gasoline mixture.
TABLE 4
15% Methanol/85% Unleaded Gasoline by Volume
Immersion Weight Change Test (gms)
Methanol - (CAS 67-56-1 )
Gasoline (CAS 8006-61-9)
Ambient 68-77 Deg. F
A C U-2000
Start 48.0 48.2 8.11
7 Days 48.6 48.8 8.13
12 Days 48.7 48.8 8.14
21 Days 48.8 48.9 8.1
28 Days 48.8 49.1 8.12
Table 5 describes the results of an ethanol immersion test wherein the same three types of floats as described in Table 4 were submerged in 100% ethanol for 28 days. The temperature during the 28-day test was between 64° and 78°F. The test measured the amount of ethanol absorbed by each float as an increase in weight of each float. Each day the floats were removed from the bath, weighed and returned to the bath.
Both the A acrylonitrile rubber float and the C acrylonitrile rubber float increased 0.2 grams in weight, while the encapsulated acrylonitrile rubber float of
this invention increased only 0.01 grams in weight.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb significant amounts of ethanol over the test period, whereas non-encapsulated floats did absorb a substantial amount of ethanol.
TABLE 5
100% Ethanol Immersion Testing Weight Change (gms)
Temperature 64-78 Deg. F
CAS 64-17-5
A C U-2000
Start 48.3 48.0 8.24
Day 7 48.5 48.4 8.27
Day 12 48.5 x 48.4 8.25
Day 21 48.5 48.4 8.26
Day 28 48.5 48.6 8.25
Turning to Table 6, which summarizes the results of a float immersion test in a 15% ethanol and 85% commercially available Regular Unleaded gasoline blend. The test measured the absorption of the ethanol gasoline blend by each float as an increase in the weight of each float over a 28-day period. This test was conducted at temperatures ranging from 64° to 78°F. The same three types of floats, as disclosed in Table 4, were utilized. Each day the floats were removed from the bath, weighed and returned to the bath.
The A non-encapsulated acrylonitrile rubber float increased 0.5 grams and the C non-encapsulated acrylonitrile rubber float increased 0.6 grams in 28 days, while the encapsulated acrylonitrile rubber float of this invention (U-2000) only increased 0.01 grams during the same time period.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb significant amounts of the ethanol/gasoline mixture over the
test period, whereas non-encapsulated floats did absorb a substantial amount of the ethanol/gasoline mixture.
TABLE 6
15% Ethanol/85% Unleaded Gasoline by Volume
Immersion Weight Change Test (gms)
Methanol- (CAS 64-15-5)
Gasoline (CAS 8006-61-9)
Ambient 68-77 Deg. F
A C U-2000
Start 48.4 48.1 8.17
7 Days 48.6 48.5 8.2
12 Days 48.6 48.5 8.19
21 Days 48.8 48.6 8.19
28 Days 48.9 48.7 8.18
Referring now to Table 7, which sets forth the results of the diesel fuel immersion test. The same three types of floats, as described in Table 4, were immersed in commercially available diesel fuel. The test was conducted at temperatures of between 64° and 78°F. for 28 days and measured the amount of diesel fuel absorbed as an increase in weight of each float. Each day the floats were removed from the bath, weighed and returned to the bath. Both the A and C acrylonitrile rubber floats increased 0.7 grams in weight while the encapsulated acrylonitrile rubber float of this invention increased 0.07 grams in weight during the 28-day test.
The conclusion drawn from this test is that the encapsulated float of this invention did not absorb significant amounts of diesel fuel over the test period, whereas non-encapsulated floats did absorb a significant amount of diesel fuel.
TABLE 7
Diesel Fuel Immersion Weight Change (gms) Test
Diesel (Ref. CAS 544-76-3)
Ambient Temperature 64-78 Deg. F
A C U-2000
Start 47.5 48.3 8.11
7 Days 48.2 49.0 8.21
12 Days 48.2 49.0 8.18
21 Days 48.2 49.0 8.22
28 Days 48.2 49.0 8.19
Table 8 sets forth the affects of a nitric acid and ammonium bifluoride mixture on encapsulated and non-encapsulated acrylonitrile rubber floats. Four separate floats were introduced into a nitric acid mixture comprised of 250 ml of 70% commercial grade nitric acid and 27 grams ammonium bifluoride. Two of the floats were commercially available non-encapsulated acrylonitrile rubber floats, denoted A and C. The other remaining floats were the encapsulated acrylonitrile rubber float of this invention, and a commercially available hollow, stainless steel float. Each float was allowed to float upon the nitric acid mixture, thus directly exposing the bottom and portions of the side of each float to the acid mixture.
TABLE 8
Acid Test
Mixture of Nitric Acid (CAS 7697-37-2) and
Ammonium Bifluoride (CAS 1341-49-7)
Mixed 250 ml 70% Commercial Grade Nitric Acid and 27 grams Ammonium
Bifluoride Ambient Temperature, Closed container, Sample Weights in Grams
Note - Test Materials Floated on Surface of Mixture, Remaining
Surfaces of Materials Exposed to Vapor
A C U-2000 Stainless Steel
Start 0.4 2.96 8.2 8.19
48 hours 0.28 2.42 8.21 8.19
96 hours 0.2 2.21 8.2 8.18
168 hours ** 1.18 8.22 8.19
336 hours ** ** 8.22 8.17
504 hours ** ** 8.22 8.16
672 hours ** ** 8.21 8.16
* - Stainless Steel Float is Innovative Fusion P/N 1012-LW, 303 stainless steel with weld. Later stage of test showed etch effect.
** - Samples failed Parts were greatly dissolved and crumbling upon failure.
After 336 hours, both of the non-encapsulated acrylonitrile rubber floats, A and C, were destroyed. The stainless steel float weighted slightly less (0.03 grams) after 672 hours; however, there were visual signs of etching of the stainless steel. The encapsulated acrylonitrile rubber float (U-2000) exhibited no weight loss after 672 hours.
The conclusion from this test is that the encapsulated float and the stainless steel float are able to withstand immersion in a nitric acid bath, whereas the non- encapsulated floats are incapable of use in this type of environment.
The above-described embodiments of the present invention are merely
descriptive of its principles and are not to be considered limiting. The scope of the invention instead shall be determined from the scope of any claims in a corresponding non-provisional application, including their equivalents.
LIST OF TABLES
Table 1 is a summary of results for Shore A hardness after a methanol soak;
Table 2 is a summary of absorption after a methanol immersion;
Table 3 is a summary of absorption after a 1 ,1 ,1 trichloroethane immersion;
Table 4 is a summary of absorption results after immersion in a 15% methanol, 85% regular unleaded gasoline mixture;
Table 5 is a summary of absorption results after an ethanol immersion;
Table 6 is a summary of absorption results after immersion in a 15% ethanol, 85% regular unleaded gasoline mixture;
Table 7 is a summary of absorption results after a diesel fuel immersion.
Table 8 is a summary of float degradation after a nitric acid/ammonium bifluoride mixture soak.
Claims
Claim:
1. A float for liquid level sensing comprising: a body including rubber material, and a protective covering for said body.
2. A float in accordance with claim 1 wherein the rubber material is synthetic rubber.
3. A float in accordance with claim 1 wherein the rubber material is acrylonitrile rubber.
4. A float in accordance with claim 1 wherein the protective covering is made of plastic.
5. A float in accordance with claim 3 wherein the protective covering is polyethylene.
6. A float in accordance with claim 3 wherein the protective covering is polypropylene.
7. A float in accordance with claim 1 wherein said protective covering is bonded to said float body.
8. A float in accordance with claim 1 wherein said float body includes a magnet therein.
9. A float in accordance with claim 1 including a guiding device extending out of said body and protective coating.
10. A float in accordance with claim 1 wherein said float body includes an insert therein.
11. A float including rubber material for liquid level sensing wherein the improvement comprises: encapsulating the body within a protective chemical-resistant plastic covering.
12. A float in accordance with claim 11 wherein the encapsulating protective covering is a preformed polyethylene container.
13. A float in accordance with claim 11 wherein the encapsulating protective covering is a preformed polypropylene container.
14. A float in accordance with claim 11 wherein the rubber material is acrylonitrile.
15. A float in accordance with claim 11 wherein the rubber material and the plastic covering are bonded.
16. A method of encapsulating a float for liquid level sensing with a protective skin comprising:
A first step, to a banbury mill mixer or the like mix by weight about
30.0% to 55.0% acrylonitrile rubber
0.5% to 4.2% zinc oxide
1.0% to 15.0% stearic acid
0.1 % to 2.0% retarder SAX salicylic acid (O-hydroxybenzoic acid) C6H4(OH) (COOH)
3.0% to 22% mistron vapor Mg3Si4O10 (OH)2
0.3% to 2.75% coumarone Indene resin absorbed on synthetic calcium
Silicate (72% cumar P-25) and
8.0% to 15.0% sulfur mix said components for between about 60 to 180 minutes while maintaining the temperature of the mixture to below about 250°F, a second step comprising taking the mixture of the first step transferring it to a suitably sized roller mill or the like and adding by weight about
12.0% to 40.0% phenolic resin (C6H6O-CH20)X
2.5% to 10.0% carbon black
0.25% to 1.5% ax Cι4H8N2S4
1.75% to 15% epoxy-resin and
1.0% to 5.0% blowing agent mixing said components for about 15 to 50 minutes while maintaining the temperature of the mixture to below about 200°F; a third step comprising transferring the mixture of the second step to a compression tool where the mixture is subjected to a pressure of about 20- 900 lbs. per cubic inch for between about 5 to 45 minutes at a temperature of between about 200°F to 350°F, removing the mixture from the compression tool and cooling a fourth step, placing a sufficient amount of the material of the third step to fill a plastic container of the desired shape and size; a fifth step of placing the plastic container into the desired finish mold tool and heating to between about 250°F. and 550°F. for between about 20 to 180 minutes to allow the acrylonitrile rubber to expand into intimate contact with the interior surface of the plastic container, whereby a rubber based float with a protective coating is produced.
17. A method as described in claim 16 wherein the mixture of the first step has a Shore A hardness of between about 15 to 90.
18. A method as described in claim 16 wherein the blowing agent is
(NO)2C3H10N4.
19. A method as described in claim 16 wherein the mixture of the second step has a Shore A hardness of between about 15 to 90.
20. A method as described in claim 16 wherein the mixture of the third step has a Shore A hardness of between about 15 to 90.
21. A method as described in claim 16 wherein a magnet may be added at step 3.
22. A method as described in claim 16 wherein an insert may be added at step 3.
23. A method as described in claim 16 wherein guides may be added at step 3.
24. A method in accordance with claim 16 wherein the mixture comprises by weight:
37.04% to 37.5% acrylonitrile rubber 0.84% to 1.01 % zinc oxide 1.67% to 2.02% stearic acid
0.21 % to 0.51 % retarder SAX salicylic acid (O-hydroxybenzoic acid) C6H4(OH) (COOH)
14.14% to 15.83% mistron vapor Mg3Si4O10 (OH)2
0.83% to 1.35% coumarone Indene resin absorbed on synthetic calcium silicate (72% cumar P-25) and
10.10% to 10.83% sulfur
22.22% to 22.50% phenolic resin (C6H6O-CH2o)X
3.33% to 4.03% carbon black
0.63% to 0.84% Altax Cι4H8N2S4
2.50% to 2.70% epoxy-resin and
3.33% to 4.04% blowing agent (NO)2C5H10N4 the mixture of the third step is subjected to a pressure of about 350 to 410 lbs. per cubic inch for between about 10 to 18 minutes at a temperature of between about 265° F to 275° F heating the mixture of the third step to between about 250°F. and 500°F. for between about 30 to 70 minutes.
25. A method in accordance with claim 24 wherein the mixture of the first step has a Shore A hardness of between about 65 to 75.
26. A method in accordance with claim 24 wherein the mixture of the second step has a Shore A hardness of between about 65 to 75.
27. A method in accordance with claim 24 wherein the mixture of the third step has a Shore A hardness of between about 65 to 75.
31
33. A product in accordance with claim 31 wherein the temperature of step B is below about 250°F.
34. A product in accordance with claim 32 wherein resin is added at step B.
35. A product in accordance with claim 31 wherein the temperature of step C is below about 200°F to 350°F.
36. A product in accordance with claim 31 wherein the temperature of step C wherein the pressure is between about 20 and 900 lbs. per cubic inch.
37. A product in accordance with claim 31 wherein a magnet is added at step C.
38. A product in accordance with claim 31 wherein an insert is added at step C.
39. A product in accordance with claim 31 wherein a guiding device is added at step C.
40. A product in accordance with claim 31 wherein the plastic container is polyethylene.
41. A product in accordance with claim 31 wherein the plastic container is polypropylene.
32
42. A product in accordance with claim 31 wherein the temperature of step E is between about 250°F. and 550°F.
43. A float for liquid level sensing having a chemically resistant protective plastic covering made by the process of:
A first step, by weight mixing
30.0% to 55.0% acrylonitrile rubber
0.5% to 4.2% zinc oxide
1.0% to 15.0% stearic acid
0.1 % to 2.0% retarder SAX salicylic acid (O-hydroxybenzoic acid) C6H4(OH) (COOH)
3.0% to 22% mistron vapor Mg3Si4O10 (OH)2
0.3% to 2.75% coumarone lndene resin absorbed on synthetic calcium
Silicate (72% cumar P-25) and
8.0% to 15.0% sulfur for between about 60 to 180 minutes while maintaining the temperature of the mixture to below about 250°F, said blended mixture to have a shore A hardness of between about 15 to 90 a second step comprising taking the mixture of the first step and adding by weight about
12.0% to 40.0% phenolic resin (C6H6O-CH20)X
33
2.5% to 10.0% carbon black
0.25% to 1.5% Altax C14H8N2S
1.75% to 15% epoxy-resin and
1.0% to 5.0% blowing agent (NO)2C5Hι0N4 mixing said components for about 15 to 50 minutes while maintaining the temperature of the mixture to below about 200°F; said blended mixture having a shore A hardness of between about 15 and 90; a third step comprising transferring the mixture of the second step to a compression tool where the mixture is subjected to a pressure of about 20- 900 lbs. per cubic inch for between about 5 to 45 minutes at a temperature of between about 200°F to 350°F, removing the mixture from the compression tool and cooling said mixture to have a Shore A hardness of between 15 to 90; a fourth step, adding to said mixture any magnets, inserts or quides; a fifth step, placing a sufficient amount of the mixture of step 3 to fill a plastic container of the desired shape and size; placing the plastic container into the desired finish mold tool and heating to between about 250°F. and 550°F. for between about 20 to 180 minutes to allow the mixture to expand into intimate contact with the interior surface of the plastic container, cool and inspect cts.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002407770A CA2407770A1 (en) | 2000-05-01 | 2001-04-28 | Encapsulated float and method for making same |
AU2001255749A AU2001255749A1 (en) | 2000-05-01 | 2001-04-28 | Encapsulated float and method for making same |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US20102200P | 2000-05-01 | 2000-05-01 | |
US60/201,022 | 2000-05-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001084092A1 true WO2001084092A1 (en) | 2001-11-08 |
Family
ID=22744159
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2001/013645 WO2001084092A1 (en) | 2000-05-01 | 2001-04-28 | Encapsulated float and method for making same |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU2001255749A1 (en) |
CA (1) | CA2407770A1 (en) |
WO (1) | WO2001084092A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005024356A3 (en) * | 2003-08-19 | 2005-05-26 | World Properties Inc | Heat-resistant foam float and method for producing the same |
WO2005045374A3 (en) * | 2003-09-05 | 2005-08-18 | World Properties Inc | Pressure-resistant foam float and method for producing the same |
KR100585942B1 (en) * | 1999-06-24 | 2006-06-01 | 제일모직주식회사 | Thermoplastic resin composition with good heat resistance and elongation property |
CN112683370A (en) * | 2020-12-31 | 2021-04-20 | 南昌工控电装有限公司 | High-temperature-resistant engine oil floater and preparation method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3874223A (en) * | 1972-10-14 | 1975-04-01 | Asahi Chemical Ind | Liquid detector |
US4229973A (en) * | 1978-03-29 | 1980-10-28 | Nifco, Inc. | Device for braking float motion in float-type liquid level gauge |
JPS62255823A (en) * | 1986-04-29 | 1987-11-07 | Toyoda Gosei Co Ltd | Liquid level measuring float |
US4756076A (en) * | 1984-10-10 | 1988-07-12 | Tokheim Comporation | Method for making a resistive level sensor |
US4862745A (en) * | 1988-07-07 | 1989-09-05 | Microdot Inc. | Fuel tank float |
-
2001
- 2001-04-28 AU AU2001255749A patent/AU2001255749A1/en not_active Abandoned
- 2001-04-28 CA CA002407770A patent/CA2407770A1/en not_active Abandoned
- 2001-04-28 WO PCT/US2001/013645 patent/WO2001084092A1/en active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3874223A (en) * | 1972-10-14 | 1975-04-01 | Asahi Chemical Ind | Liquid detector |
US4229973A (en) * | 1978-03-29 | 1980-10-28 | Nifco, Inc. | Device for braking float motion in float-type liquid level gauge |
US4756076A (en) * | 1984-10-10 | 1988-07-12 | Tokheim Comporation | Method for making a resistive level sensor |
JPS62255823A (en) * | 1986-04-29 | 1987-11-07 | Toyoda Gosei Co Ltd | Liquid level measuring float |
US4862745A (en) * | 1988-07-07 | 1989-09-05 | Microdot Inc. | Fuel tank float |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100585942B1 (en) * | 1999-06-24 | 2006-06-01 | 제일모직주식회사 | Thermoplastic resin composition with good heat resistance and elongation property |
WO2005024356A3 (en) * | 2003-08-19 | 2005-05-26 | World Properties Inc | Heat-resistant foam float and method for producing the same |
WO2005045374A3 (en) * | 2003-09-05 | 2005-08-18 | World Properties Inc | Pressure-resistant foam float and method for producing the same |
CN112683370A (en) * | 2020-12-31 | 2021-04-20 | 南昌工控电装有限公司 | High-temperature-resistant engine oil floater and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
AU2001255749A1 (en) | 2001-11-12 |
CA2407770A1 (en) | 2001-11-08 |
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