WO1993023472A1 - Gels - Google Patents

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Publication number
WO1993023472A1
WO1993023472A1 PCT/GB1993/000953 GB9300953W WO9323472A1 WO 1993023472 A1 WO1993023472 A1 WO 1993023472A1 GB 9300953 W GB9300953 W GB 9300953W WO 9323472 A1 WO9323472 A1 WO 9323472A1
Authority
WO
WIPO (PCT)
Prior art keywords
ethylene
composition according
weight
propylene
styrene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/GB1993/000953
Other languages
English (en)
French (fr)
Inventor
Philip James Hammond
John Michael Hudson
Hendrik Graulus
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Raychem Ltd
Original Assignee
Raychem Ltd
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
Priority claimed from GB929210291A external-priority patent/GB9210291D0/en
Priority claimed from GB929214425A external-priority patent/GB9214425D0/en
Priority to CA002133763A priority Critical patent/CA2133763C/en
Application filed by Raychem Ltd filed Critical Raychem Ltd
Priority to KR1019940704020A priority patent/KR950701663A/ko
Priority to US08/335,784 priority patent/US5618882A/en
Priority to EP93910172A priority patent/EP0640115B1/en
Priority to JP51997693A priority patent/JP3642785B2/ja
Priority to DE69320041T priority patent/DE69320041T2/de
Priority to BR9306346A priority patent/BR9306346A/pt
Publication of WO1993023472A1 publication Critical patent/WO1993023472A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/0016Plasticisers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L53/02Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes

Definitions

  • This invention provides new and technically superior gel compositions comprising a styrene-(ethylene/propylene)-styrene (SEPS) block copolymer and at least 300 parts by weight (preferably at least 400 parts by weight, more preferably at least 500 parts by weight) of extender liquid per 100 parts by weight of the block copolymer, which liquid extends and softens the ethylene/propylene polymer blocks of the said copolymer.
  • SEPS styrene-(ethylene/propylene)-styrene
  • Gels according to the present invention made of SEPS copolymer having weight average molecular weight Mw of at least 180,000, preferably at least 200,000, more preferably at least 220,000, and polystyrene content of 25-45 weight percent, preferably 28-40 weight percent, more preferably 29 to 36 weight percent, and made with substantially non-aromatic extender liquid, tend to have improved high-temperature performance and improved ability to retain the extender liquid when subjected to pressure in various end uses.
  • the SEPS gels of this invention also tend to have higher tack than the known SEBS gels r thus reducing the need for added tackifiers to achieve a desired level of adhesion to surfaces with which they are in contact in end use.
  • the SEPS gels are preferably soft, high-temperature-slump- resistant, springy gel compositions, by which is meant liquid-extended polymer compositions having an ultimate elongation (measured by ASTM D412 modified as described below) greater than 100%. with substantially elastic deformation (i.e. substantially no hysteresis) to an elongation of at least 100%; ultimate tensile strength (ASTM D412) less than 1 MegaPascal; dynamic storage modulus (as hereinafter described) less than 50000 Pascals; and substantially zero slump at temperatures up to 100°C, preferably up to 120°C, more preferably up to 135°C, and especially up to 150°C.
  • liquid-extended polymer compositions having an ultimate elongation (measured by ASTM D412 modified as described below) greater than 100%. with substantially elastic deformation (i.e. substantially no hysteresis) to an elongation of at least 100%; ultimate tensile strength (ASTM D412) less than 1 Mega
  • the invention for some end purposes is more particularly concerned with such gel compositions comprising from 4% to 20% by weight of the SEPS copolymer and at least 500 parts by weight of extender liquid per 100 parts by weight of the polymer, in which the SEPS copolymer comprises more than 50%, preferably more than 75%, more preferably more than 90%, and especially more than 95%, by weight, or substantially all, of the total gelling polymer present.
  • Various additives may be present, for example the tackifiers described in WO-A-9005166 or the polyphenylene oxide described in WO-A- 8800603, or styrene-alkylene di-block copolymers for reducing the loss of extender liquid as described in our co-pending British Application 9119261.7.
  • the superior performance of the present SEPS gels may reduce or eliminate the need for such additives.
  • the SEPS gels with which the present invention is concerned, are well suited, inter alia, for re-enterable sealing of electrical connection enclosures.
  • the gels are subjected to continuous pressure, in view of which their ability to retain the extender liquid is important.
  • the composition may-be "substantially free of polystyrene- compatible components which significantly raise or lower the softening temperature (Ts) of the composition, either in the sense that substantially no such components are present, or in the sense that the quantities of such components which are present are not sufficient to produce a significant effect on the softening temperature.
  • Ts softening temperature
  • TTie use of such components significantly to raise the softening temperature (Ts) is claimed in the aforementioned WO-A-8800603 and may be used in the present case.
  • Lowering of Ts is generally undesirable for the present purposes, and the extender oil will therefore preferably be substantially non-aromatic, meaning that it contains less than 2%, more preferably less than 1%, and especially substantially zero, aromatic material.
  • SEPS gels according to the present invention provide improvements in slump-resistance at elevated temperatures compared with similar SEBS gels, while still achieving desirable "softness” and “springiness". Slumping usually occurs some tens of degrees above the onset of softening temperature Ts.
  • the present gels are thus clearly distinguished from known cable-filling materials which are designed to slump and flow in use.
  • the compositions of this invention remain substantially stable, homogeneous, and relatively free from exudation of extender, and various properties are improved while maintaining an adequate balance of other properties.
  • the gel compositions when adhered to another surface, or to themselves, tend to be removable cleanly by adhesive release at the contact interface, substantially without any cohesive failure within the body of the gel composition.
  • SEPS block copolymers for the purposes of this invention are those wherein the copolymer comprises 25 to 45 weight percent, preferably 28 to 40 weight percent, especially 29 to 36 weight percent, of the polystyrene blocks.
  • the block copolymer preferably comprises 75 to 55 weight percent, more preferably 72 to 60 weight percent, especially 71 to 64 weight percent, of the polyalkylene blocks.
  • the polyalkylene blocks preferably comprise substantially fully hydrogenated poly(ethylene/propylene) blocks, especially those predominantly (e.g. >90% or >95%) comprising units of formula -(CH2 CH (CH3) CH2 CH2)- possibly with small amounts of isomers such as
  • the polyalkylene blocks have Mw of at least 125,000, more preferably at least 130,000, especially at least 140,000.
  • the proportions of ethylene/propylene units incorporated in the polyalkylene blocks may be varied from as low as 20% to 100%, proportions of less than 100% being preferably derived from a mixed isoprene/butadiene feedstock which is copolymerised and hydrogenated to produce the SEPS triblocks having mixed ethylene/propylene : ethylene/butylene polyalkylene blocks.
  • the benefits of the SEPS gels described in the aforementioned pending application are produced by the presence of the ethylene/propylene units, and increasing proportions of at least 30% or 40%, preferably at least 50%, of the ethylene/propylene units are preferred.
  • a particularly preferred SEPS block copolymer for the present purposes has polyalkylene mid-blocks comprising about 60% ethylene/propylene units and about 40% ethylene/butylene units. Higher proportions of ethylene/propylene units, such as 80% and 90%, and single-unit alkylene blocks of 100% ethylene/propylene units are also useful. Proportions are percentages by weight.
  • alkylene units other than ethylene/butylene could be incorporated with the ethylene/propylene units to form other useful SEPS block copolymers, but ethylene/butylene is preferred.
  • Cross-linking of the composition although not essential, may be effected if desired as described in WO-A-8800603 and EP-A- 0224389, and may produce further improvements in properties.
  • the extender liquids useful in the compositions of this invention comprising the block copolymer may be selected from oils conventionally used to extend elastomeric materials.
  • the oil may be hydrocarbon oil such as paraffinic or naphthenic oils, synthetic oils such as polybutene oils, and mixtures thereof.
  • the preferred oils are substantially non-aromatic mixtures of paraffinic and naphthenic hydrocarbons.
  • the oils preferably have a minimum boiling point higher than the softening point of the block copolymer(s) and any additional polymer or copolymer.
  • the extender liquid preferably comprises a substantially non-aromatic paraffinic /naphthenic mineral oil of paraffinic:naphthenic (P:N) carbon ratio within the range from 1.75:1 to 5:1, preferably 1.77:1 to 3:1, more preferably 1.9:1 to 2.7:1, and most preferably 2.2:1 to 2.4:1, this extender oil being preferred for all the gel compositions herein described.
  • P:N paraffinic:naphthenic
  • the oil has a relative density at 20°C according to ASTM D1298 within the range from 0.861 to 0.865, preferably 0.862 to 0.864.
  • Preferred extender oils include, for example, those available from Fina Chemicals under the Trade Marks 'Vestan A360B" (preferred) from Fina. "Drakeol 34" from Penreco, and “Witco 380PO” from Witco.
  • compositions of this invention are preferably prepared by mixing the oil with the block copolymer(s) at a temperature not less than the glass transition temperature of the polystyrene blocks of the SEPS block copolymer, as described generally in WO-A-8800603. Mastication or other mixing techniques at lower temperatures, perhaps with the aid of volatile solvents, may however be used if the resulting composition is acceptable for the intended end use.
  • compositions according to the various aspects of this invention can be made having a wide range of physical properties. such as dynamic storage modulus, ultimate elongation, and tear strength, to suit particular end use requirements.
  • the preferred compositions having an ultimate elongation of at least 200% (ASTM D412) are particularly useful as sealing materials.
  • the compositions preferably contain more than 500, and preferably not more than 5000, parts by weight of extender liquid per 100 parts by weight of the block copolymer.
  • additives may be stabilisers, antioxidants, flame retardants, tackifiers, corrosion inhibitors and the like. It is useful to use antioxidants in all the compositions of this invention.
  • compositions of this invention have numerous uses as elastomeric materials and in particular may be used as sealing materials for electrical connection enclosures, for example as illustrated in published European Patent application 0108518 and 0191609 (the disclosures of which are both incorporated herein by reference), although the compositions of this invention will have many and varied uses depending on the properties desired and the temperatures to be encountered.
  • Gel or gelloid compositions within the scope of this invention are preferably defined by the criteria (1) to (8) derived from Tests I to V as described in WO-A-8800603, the disclosure of which is . incorporated herein by reference, of which criteria preferably not more than one (not (1) or (2)) will be outside the specified ranges.
  • the preferred SEPS block copolymers for the present invention are selected from those commercially available under the Trade Mark “SEPTON” from Kuraray of Japan, SEPTON 4055 being the aforementioned preferred grade.
  • SEPTON 4055 being the aforementioned preferred grade.
  • the presence in a given composition of the required range of properties for optimised gel compositions according to the present invention may be determined by simple trial and error against the aforementioned criteria. Examples of the SEPS gels according to this invention will now be described in comparison with corresponding SEBS gels made from the known polymer available under the Trade Mark KRATON G1651.
  • the weight average molecular weights (Mw) were determined by gel permeation chromatography (GPC) under the following conditions:
  • Solvent HPLC grade THF. Flow rate : 1.33 mls/min Temperature : ambient. Injection volume : 200 microlitres Sample cone. : 0.05% Internal std. : phenyl hexane Detector : Differential Refractive Index detector Columns : 2 off 60 cms Polymer Labs, mixed gel - 10 micron. DATA REDUCTION : Polymer Laboratories Caliber Software.
  • the samples (100 mg) were accurately weighed and dissolved in 40 mis of THF in 50 ml volumetric flasks. 50 microlitres of marker were added then the polymer had dissolved, and the solutions up made to the 50 ml mark. They were then filtered through a 0.2 micrometre pressure filter, and injected into the GPC. Four separate solutions of differing mixtures of polystryrene standards were made up in volumeric glassware, and spiked with a known volume of marker.
  • the marker was used to correct for flow variations. " The software created a calibration curve from the mixtures of standards using a third order polynomial fit.
  • TMA softening point test a weighted piston is placed on top of a gel sample. The sample is then heated, and the deflection of the probe measured as a function of temperature. The trace produced has a flat, linear region (A), followed by a transition (melting) region (B) followed by a second flat region (C) where the piston has reached the limit of its travel. This is shown schematically in the accompanying Figure 1.
  • the quoted softening point Ts is the temperature where extrapolated straight lines through A and B intersect.
  • TMA- 942 Du Pont thermomechanical analyser
  • Du Pont 1090 thermal analyser A 2.54 mm diameter flat- bottomed quartz probe was used with a 2g load.
  • the gel sample was a disc, 6.25mm in diameter and 2mm thick.
  • the sample was equilibrated at -40°C for 5 minutes, then heated to 300°C at a rate of 5°C/minute.
  • Tensile and elongation testing was according to ASTM D412. except that BS 903 Type 2 dumb-bells with a gauge length of 40mm were used. The pulling speed was lOOmm/minute.
  • G' (modulus) and tan delta were measured using a Bohlin VOR- melt rheometer and software.
  • the rheometer was used in oscillation mode, with a 25mm diameter parallel plate measuring system and a 90 gem torsion bar transducer. Gel samples were 25mm diameter discs, of thickness 3 ⁇ 0.2mm. Measurements were made at approximately 23°C, at oscillation frequencies of 0.1 Hz and 1 Hz. The instrument was run at its maximum angular strain, corresponding to a strain of about 6% in these samples.
  • Sample discs of gel (15mm diameter x 3mm thickness) were supported inside 15mm diameter holes cut in a metal block. The lower surface of each disc was supported on a fine mesh, to provide free surface for extender loss. A constant pressure of 50kPa was applied to the top surface by means of a weighted piston. The whole assembly was placed in an oven at 60°C, and the weight loss from each disc monitored with time. The M (infinity) value quoted is the mass of extender lost at equilibrium, expressed as a percentage of the original mass.
  • KRATON G 1701 is a styrene-ethylene/propylene diblock copolymer which improves the oil retention of KRATON G1651 gels as described in our aforementioned copending British Patent Application. This table illustrates that:
  • Tensile strength and elongation show a general improvement, especially for EP/EB midblocks.
  • the performance of the gels as sealants is indicated by measurement of tan delta and tack, as follows. Tan delta is measured by the dynamic oscillatory shear test using the aforementioned rheometer. and represents the ratio of the applied energy dispersed by viscous processes to the energy stored in the deformed elastic polymer network. Higher tan delta values indicate an increase in the internal viscous damping within the gel, which manifests itself as improved ability to conform to surfaces with which the gel is brought into contact. When the surface is one which the gel composition can "wet", the result is an increase in tack or adhesion, which may be qualitatively perceived as increased stickiness to touch.
  • Tack may be measured in terms of the work done in pulling a probe away from a gel sample with which it has been pressed into contact.
  • the equipment used is a Stevens-LFRA Texture Analyser, which is a mechanical device for pushing a probe a fixed distance into a material and subsequently withdrawing it.
  • the probe is attached to a bi-directional load cell, which measures the normal force at the probe surface during the test.
  • Various probes may be used, and the speed and depth of penetration may be controlled by the operator.
  • the gel sample was a moulded slab, 150mm x 150mm x 3mm thick.
  • the output from the load cell is directed to a recording device, which may be a chart recorder or a digital computer.
  • a recording device which may be a chart recorder or a digital computer.
  • the data was output to an IBM Personal Computer running software supplied by Stevens.
  • the resulting force-time curve has a positive part, where the probe is being pushed into the gel, followed by a negative part where the probe is being withdrawn.
  • the area under the negative part of the curve is a measure of the work done in withdrawing the probe, which is approximately equal to the total integrated work of overcoming the adhesion.
  • This "tack area” has units of grammes x seconds. Higher values correspond to tackier gels.
  • Table III shows compression set measured according to ASTM D395 - 89 Method B at 70°C.
  • gels including PPO are measured at 90°C. This is because the PPO gels show negligible set at 70°C.
  • the ASTM method specifies 50°C, but most gels show negligible set at this temperature.
  • the gels according to the present invention may contain additives compatible with the polystyrene end blocks of the gel copolymer, which raise the softening temperature and other performance characteristics of the gel, for example polyphenylene oxide (PPO) as described in WO-A-8800603.
  • PPO polyphenylene oxide
  • the gels may contain additives which resist migration into the gel of PVC plasticisers from PVC articles with which the gel is in contact use, for example the phosphate additives or other additives described in WO-A-9105014.
  • the invention also provides devices wherein a body of the gel composition according to this invention forms a seal between two or more surfaces; and devices, preferably enclosures for electrical connections, comprising a body of the present gel composition and means for holding the body of gel composition under compression in use, preferably against and -around the connections, so as to form a seal against contamination and/or corrosion.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Cosmetics (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Sealing Material Composition (AREA)
PCT/GB1993/000953 1992-05-13 1993-05-10 Gels Ceased WO1993023472A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
BR9306346A BR9306346A (pt) 1992-05-13 1993-05-10 Géis
DE69320041T DE69320041T2 (de) 1992-05-13 1993-05-10 Gele
CA002133763A CA2133763C (en) 1992-05-13 1993-05-10 Gels
KR1019940704020A KR950701663A (ko) 1992-05-13 1993-05-10 겔(gels)
US08/335,784 US5618882A (en) 1992-05-13 1993-05-10 Gels containing SEPS block polymers
EP93910172A EP0640115B1 (en) 1992-05-13 1993-05-10 Gels
JP51997693A JP3642785B2 (ja) 1992-05-13 1993-05-10 ゲル

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB9210291.2 1992-05-13
GB929210291A GB9210291D0 (en) 1992-05-13 1992-05-13 Gels
GB9214425.2 1992-07-07
GB929214425A GB9214425D0 (en) 1992-07-07 1992-07-07 Gels

Publications (1)

Publication Number Publication Date
WO1993023472A1 true WO1993023472A1 (en) 1993-11-25

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1993/000953 Ceased WO1993023472A1 (en) 1992-05-13 1993-05-10 Gels

Country Status (16)

Country Link
US (1) US5618882A (https=)
EP (1) EP0640115B1 (https=)
JP (1) JP3642785B2 (https=)
KR (1) KR950701663A (https=)
CN (1) CN1052495C (https=)
AT (1) ATE169048T1 (https=)
AU (1) AU675646B2 (https=)
BR (1) BR9306346A (https=)
CA (1) CA2133763C (https=)
DE (1) DE69320041T2 (https=)
ES (1) ES2118956T3 (https=)
MX (1) MX9302771A (https=)
MY (1) MY113264A (https=)
NZ (1) NZ252225A (https=)
TR (1) TR28612A (https=)
WO (1) WO1993023472A1 (https=)

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ATE169048T1 (de) 1998-08-15
EP0640115B1 (en) 1998-07-29
DE69320041T2 (de) 1999-04-22
KR100290060B1 (https=) 2001-09-17
CN1052495C (zh) 2000-05-17
MY113264A (en) 2002-01-31
TR28612A (tr) 1996-11-14
JP3642785B2 (ja) 2005-04-27
JPH07506614A (ja) 1995-07-20
BR9306346A (pt) 1998-06-30
AU675646B2 (en) 1997-02-13
CA2133763A1 (en) 1993-11-25
DE69320041D1 (de) 1998-09-03
AU4078093A (en) 1993-12-13
ES2118956T3 (es) 1998-10-01
NZ252225A (en) 1996-04-26
CA2133763C (en) 2004-04-13
US5618882A (en) 1997-04-08
EP0640115A1 (en) 1995-03-01
MX9302771A (es) 1994-05-31
CN1080938A (zh) 1994-01-19
KR950701663A (ko) 1995-04-28

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