WO2001044400A1 - Low outgassing pressure sensitive adhesives and method of use - Google Patents

Low outgassing pressure sensitive adhesives and method of use Download PDF

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Publication number
WO2001044400A1
WO2001044400A1 PCT/US2000/027260 US0027260W WO0144400A1 WO 2001044400 A1 WO2001044400 A1 WO 2001044400A1 US 0027260 W US0027260 W US 0027260W WO 0144400 A1 WO0144400 A1 WO 0144400A1
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WO
WIPO (PCT)
Prior art keywords
psa
elastomer
styrene
scavenger
block copolymer
Prior art date
Application number
PCT/US2000/027260
Other languages
French (fr)
Inventor
Huimin Yang
Original Assignee
Brady Worldwide, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Brady Worldwide, Inc. filed Critical Brady Worldwide, Inc.
Publication of WO2001044400A1 publication Critical patent/WO2001044400A1/en

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Classifications

    • GPHYSICS
    • G11INFORMATION STORAGE
    • G11BINFORMATION STORAGE BASED ON RELATIVE MOVEMENT BETWEEN RECORD CARRIER AND TRANSDUCER
    • G11B33/00Constructional parts, details or accessories not provided for in the other groups of this subclass
    • G11B33/14Reducing influence of physical parameters, e.g. temperature change, moisture, dust
    • G11B33/1446Reducing contamination, e.g. by dust, debris
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J153/00Adhesives based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
    • C09J153/02Vinyl aromatic monomers and conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J153/00Adhesives based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
    • C09J153/02Vinyl aromatic monomers and conjugated dienes
    • C09J153/025Vinyl aromatic monomers and conjugated dienes modified
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2170/00Compositions for adhesives
    • C08G2170/40Compositions for pressure-sensitive adhesives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02Organic macromolecular compounds, natural resins, waxes or and bituminous materials

Definitions

  • This invention relates to pressure sensitive adhesives (PSA). More particularly,
  • this invention relates to PSA's for use with computer devices, and to methods for
  • cleaner computer devices such as cleaner data storage devices.
  • plastics, elastomeric, and ceramic parts containing various lubricants and a variety of
  • Pressure sensitive adhesives were used for various applications such as seals,
  • a typical drive may include
  • At least one component which bears a PSA e.g., a tape, which was used to hold the
  • Adhesive materials can deposit contaminants on disk and
  • anions particularly, chloride and sulfate ions
  • outgassing which can result in stiction
  • impurities used to dissolve and coat polyacrylate PSA's can be a problem if not
  • cleaning methods were either aqueous cleaning, solvent cleaning, or carbon dioxide cleaning. All of these cleaning methods
  • the second strategy used by the disk drive industry was to use parts and processes
  • a typical limit for outgassed materials may be as low as 2500 nanograms per square
  • centimeter centimeter (ng/cm 2 ); the limit for anions may be a maximum of 800 ng/cm 2 .
  • This invention relates to a
  • microcontaminants was present around the disk drive.
  • the invention comprises an improved PSA comprising:
  • the invention comprises an improved method for preparing a computer device which includes at least one component bearing a PSA, the
  • the resin includes at least one impurity, the impurity comprising a compound
  • the invention comprises a computer device comprising
  • PSA at least one component containing a PSA, wherein the PSA comprises:
  • C. at least one scavenger C. at least one scavenger.
  • styrenic refers to mono-alkenyl arenes.
  • styrenic polymer or copolymer was formed by the polymerization of at least one mono-
  • a "block copolymer” was a polymer containing long stretches of two or more
  • polymer structure was attached to a block(s) of another type of polymer structure.
  • diblock copolymer was a block copolymer that has the general structure A-B, where A
  • a "triblock copolymer” was a block copolymer that has the
  • a "tackifying resin” was a resin that, when added to a rubber or an elastomer, the
  • composition has the properties of a pressure sensitive adhesive.
  • Pressure sensitive adhesives were permanently and aggressively tacky (sticky) solids which form
  • Tack can be quantified as the force required to separate an adherend
  • Tack can be measured by using the ASTM D-2979
  • a "scavenger” was a substance added to a system or mixture to consume or
  • hydrocarbon resin was a resin in the number molecular weight range of a few
  • hydrocarbonaceous materials such as petroleum, coal, tar, and turpentine.
  • An improved computer device was prepared by preparing at least one adhesive as
  • the component was a film, tape or label which was used to seal or
  • the computer device was
  • a disk drive or other data storage device preferably a disk drive or other data storage device.
  • the adhesive used in this invention comprises (i) at least 10, preferably at least 40,
  • weight percent of a tackifying resin 60, weight percent of a tackifying resin, and, (iii) at least 0.1 , preferably at least 2, more
  • the PSA of this invention comprises polymers typically known in the art of
  • such polymers impart an elastic or viscoelastic property to the
  • Polymers that were useful for the PSAs of this invention include rubbers, such as
  • Block copolymers were well-known in the field of PSAs. Any one of these well-known
  • block copolymers typically take on the general configuration A-B-A or A-B-A-
  • each "A" block which was generally characterized as an end block, was a
  • thermoplastic polymer block prepared by a polymerization of a styrenic monomer such as
  • styrene a-methyl-styrene, tert-butyl-styrene, and vinyl-toluene.
  • SBS styrene-isoprene-styrene block copolymer
  • SIS styrene-ethylene butyl ene-styrene
  • SEBS block copolymer
  • SEPS styrene-ethylene propylene-styrene
  • block copolymers was between 10,000 and 500,000, expressed as number average
  • the block copolymer of this invention was a hydrogenated block
  • the hydrogenated block copolymer was preferably a block copolymer of
  • polystyrene and a polydiene typically selected from the group consisting of
  • polybutadiene or polyisoprene was hydrogenated to yield a saturated mid block.
  • the block copolymers of this invention comprise styrene end
  • the block copolymer has end blocks of styrene whose number
  • average molecular weight was in the range of 10,000 to 30,000, and the mid block was a
  • SEPS propylene-styrene copolymers
  • the KRATON® G hydrogenated block copolymers have a number average
  • M n molecular weight
  • the block copolymer, in combination with the tackifying resin(s), outgasses less than 1500 ng/cm 2 as measured by
  • polymer can be reduced by applying removal means to the polymer prior to the
  • Such removal means can comprise extreme high temperature drying,
  • Polyurethanes were thermoplastic polymers produced by the condensation
  • polyesters containing hydroxyl groups The basic polymer unit was formed as shown in
  • R, and R 2 were hydrocarbon radicals or substituted hydrocarbon radicals.
  • Natural rubber was a well-known material. Natural rubber was a polyisoprene
  • Natural rubber can also be made synthetically.
  • Acrylate copolymers were known in the art. Such acrylic adhesives were discussed in U.S.P. 5,981,666.
  • Tackifying resins of this invention were resins that associate predominantly with
  • the mid block in that between 100 and 200 or more parts by weight of the mid block
  • tackifying resins can be reduced by applying removal means to the tackifying resins prior
  • Such removal means can comprise extreme high temperature
  • tackifying resins examples include
  • polyhydric esters of rosin or hydrogenated rosin esters such as glycerol and
  • polyhydric alcohol synthetic polyterpenes, terpene-olefin copolymers, terpene-phenols,
  • tall oil rosin, synthetic saturated hydrocarbon resins such as saturated alicyclic
  • hydrocarbons hydrocarbons, olefinic resins, aromatic containing resins, phenol-aldehyde resins, a-
  • pinene resins a-pinene resins, terpene-phenolic resins, and copolymers such as of 1 ,3-
  • the preferred tackifying resin of this invention was of the type known as
  • hydrocarbon resins A good description of hydrocarbon resins can be found in Kirk-
  • te ⁇ ene resins i.e., polymers with (repeating) isoprene (C 5 H 8 ) or
  • Te ⁇ ene-phenols were also produced.
  • Aromatic monomers useful in forming the aromatic containing resin compositions are:
  • styrenic monomers e.g., styrene, a-methylstyrene, vinyl toluene,
  • Aliphatic tackifying resins can be made by polymerizing a feed stream containing
  • Such feed streams can contain other aliphatic unsaturated monomers such as
  • Mixed aliphatic aromatic resins contain sufficient aromatic monomers and sufficient aliphatic monomers to produce a resin having both aliphatic and aromatic
  • the preferred tackifying agents were hydrogenated to C, 2 resins,
  • aromatic tackifying resins include styrenated te ⁇ ene resins,
  • the tackifying resin was derived by the polymerization and
  • polymerization can interfere with the recording, storage or reading of data in a computer
  • the tackifying resin of this invention was low molecular weight
  • the tackifying resin was at least one of
  • pure hydrocarbons may be tolerated to a relatively higher level than that of the chemicals containing reactive moieties, such as acid, alcohol
  • Some of these chemicals containing reactive moieties can be substantially
  • This invention reduces the level of these chemicals that was outgassed, from a
  • reaction was a reaction between reactive groups on the scavengers and reactive moieties
  • the anchoring reaction was typically conducted in a solution prepared by
  • a suitable liquid such as, e.g., toluene.
  • the scavengers of this invention react with impurities, such as acids, amines
  • the products resulting from this achoring reaction must be non- volatile even at elevated temperatures such as 85 °C.
  • the scavengers must be compatible with the PSA system.
  • Typical scavengers of this invention were low molecular weight compounds and
  • Mixtures of scavengers can provide for the capture of
  • the scavengers of this invention have moieties that react with the polar
  • reactive moieties such as acid, alcohol, amine, etc.
  • scavengers usable in this invention include polyisocyanates,
  • Preferred scavengers were polyisocyanates and aluminum oxide.
  • Suitable polyisocyanates include the DESMONDURTM series polymers
  • DESMONDURTM 3390 DESMONDURTM 3300 and DESMONDURTM 3390 have the same
  • the PSA of this invention was conveniently prepared by adding at least 0.1 ,
  • the PSA's of this invention can optionally include other components known in the
  • These components can include plasticizing oils, resin modifiers, and antioxidants.
  • nonvolatile organic liquids and low-melting solids e.g., phthalate, adipate, and sebacate
  • esters such as ethylene glycol and its derivatives, tricresyl phosphate, castor oil,
  • Antioxidants in particular can be harmful
  • PSA's examples include, inter alia:
  • Hot-melt compounding (any of methods i-iii, above) was not a favored
  • PSA outgasses less than 1500 ng/cm 2 as measured by Modified IDEMA M l 1 -98.
  • the PSA of this invention was formed by dissolving the mixtures in
  • these solutions contain at least 10, more preferably at least 20, most preferably
  • Suitable organic solvents must be inert to the block copolymer and the tackifying
  • the organic solvent must be selected such that substantially all of the solvent can be evaporated from the PSA. “Substantially all of the solvent” refers to removal of the solvent such that the residual levels of solvent were less than 5 percent,
  • Preferred organic solvents include toluene, cyclohexane and heptane, more preferably
  • the solution can be filtered or decanted after the scavenging reaction
  • absorbent was used as a scavenger.
  • the solvent can be evaporated from the PSA by any technique known in the art,
  • the polymer was at least one of a
  • At least one scavenger wherein at least one of the polymer or the tackifying resin includes at least one impurity, the impurity comprising a compound
  • the substrate of the steps D and E, above was a
  • component of a computer device more preferably, a component of a computer data
  • the permanent and expendable equipment (Section 2) consists of a: (a) Type 303
  • thermal deso ⁇ tion tubes were conditioned at 320 °C for 8 minutes. Deso ⁇ tion tubes were installed and the samples were placed in the sample outgassing chambers. The
  • sample chamber flow rate was set at approximately 50 milliliters per minute (ml/min.)
  • the outgassing chamber was continuously heated at 85
  • the desorber was programmed to desorb at 320 °C for 8 minutes at 50 ml/min.
  • cold trap was set at -30 °C and desorbed at 350 °C, with a hold time of 8 minutes, and
  • valve and line temperatures set at 200°C.
  • the outlet split was set at 54 ml/min.
  • sample split ratio was approximately 49: 1.
  • the gas chromatograph flow rate was
  • MORESTER 49007 is a registered trademark owned by Morton international which was added as a modifier but has no eftect on the final properties of the adhesive
  • a scavenger substantially decreases, by at least 16 percent, the amount of
  • a comparative example (E) was prepared by dissolving
  • polyproplene film available from DuPont Preferably, the solution was uniformly
  • ESTANE® is a trademark of BF Goodrich.

Abstract

An improved pressure sensitive adhesive (PSA), comprising at least one polymer selected from natural rubber, styrenic-elastomer copolymers, acrylate copolymers, polyurethanes or combinations thereof; and at least one tackifying resin, was disclosed which uses a scavenger to capture impurities inherent in the polymer and/or the tackifying resin. Additionally, a method for making improved, cleaner computer devices by using the improved PSA on computer device components that contain a PSA. The component thus produced was ideally suited to be used in disk drives. Also disclosed were computer devices, preferably computer data storage devices, made by the method disclosed.

Description

LOW OUTGASSING PRESSURE SENSJTINE ADHESIVES AND METHOD OF USE
This invention relates to pressure sensitive adhesives (PSA). More particularly,
this invention relates to PSA's for use with computer devices, and to methods for
preparing cleaner computer devices, such as cleaner data storage devices.
Computer disk drives were complex assemblages of surface treated alloys,
plastics, elastomeric, and ceramic parts containing various lubricants and a variety of
adhesives. Pressure sensitive adhesives were used for various applications such as seals,
labels, damping, etc. in today's computer data storage devices. The use of PSA's has been
an effective means of lowering unit cost for storage devices. A typical drive may include
at least one component which bears a PSA, e.g., a tape, which was used to hold the
housing of the disk drive together.
Demand for increased storage capacity of disk drives has produced product
designs requiring a higher level of concern for adhesive contamination. New disk drive
technology, such as decreasing flying heights, use of magneto-resistive head technology,
and pseudo-contact recording, have improved the performance and capacity of disk drive
components. Use of this new technology has also left the disk drive more susceptible to
damage from environmental factors. Building drives with contaminated or outgas-prone
parts can result in stiction/wear and functional problems, including electrical error issues
from thermal asperities.
The cleanliness of PSA materials has been a concern for disk drive engineers.
Physical contamination such as dust particles, skin flake, and moisture, along with
possible chemical contamination by the materials used in the PSA, can affect the drive life or reliability of the device. Adhesive materials can deposit contaminants on disk and
reading heads and cause reading problems or disk crashes.
Specific ions and organic tins were particularly harmful to heads and disks. Small
levels of chlorine containing materials have been identified to be responsible for disk
corrosion. Organic materials capable of undergoing polymerization were unacceptable at
very low levels. Organic or inorganic acids or bases can corrode the sensitive layers of
the storage disk. Typical types of microcontamination commonly found in the disk drive
industry include organic contamination that can cause stiction; corrosion from residual
anions (particularly, chloride and sulfate ions); outgassing, which can result in stiction;
and airborne particulates.
Polyacrylate-based PSA's have been used extensively in the components for disk
drives. A select few were considered useable; none were totally satisfactory. The chemical byproducts from the initiators used in the initial polymerization of acrylates can
be unacceptable even at relatively low levels in disk drives. The solvents and their
impurities used to dissolve and coat polyacrylate PSA's can be a problem if not
thoroughly dried from the finished adhesive coating. Most polyacrylate pressure sensitive
adhesives must be chemically cross-linked to provide the necessary performance
characteristics. The chemicals used for, or byproducts produced from, the cross-linking
can be unacceptable or at unacceptable levels. The levels of unreactive monomers and
their impurities in polyacrylate PSA's have been known to cause drive failures.
The disk drive industry was resorting to two strategies in order to minimize the
presence of microcontaminants in the environment of the disk drive. The first strategy
was to use one of a variety of cleaning methods in order to remove the microcontaminants
from the finished disk drive parts. Typically, such cleaning methods were either aqueous cleaning, solvent cleaning, or carbon dioxide cleaning. All of these cleaning methods
have their advantages and difficulties. However, no cleaning method can remove all
contaminants. Cleaning was a percentage removal process, and it targets specific
contaminants. The higher the initial level of contaminants, the higher the final level of
contaminants in the finished product.
The second strategy used by the disk drive industry was to use parts and processes
that contain or produce fewer contaminants. These more stringent specification
requirements were a challenge to the suppliers of components for the disk drive industry.
Specific requirements include low outgassing and low ionic contamination. For example,
a typical limit for outgassed materials may be as low as 2500 nanograms per square
centimeter (ng/cm2); the limit for anions may be a maximum of 800 ng/cm2.
Further disclosure on microcontaminants in the disk drive industry can be found in
Peter Mee et al, Management of Disk Drive Component Microcontamination. IDEMA® Insite, Vol. IX, No. 2 (March/April 1997).
It has been a difficult challenge for the adhesive industry to meet the requirements
of the disk drive engineers with polyacrylate adhesives. This invention relates to a
method for preparing a computer device in a manner that a lower level of
microcontaminants was present around the disk drive.
In one embodiment, the invention comprises an improved PSA comprising:
A. at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof;
B. at least one tackifying resin; and
C. at least one scavenger. In another embodiment, the invention comprises an improved method for preparing a computer device which includes at least one component bearing a PSA, the
method comprising the steps of:
A. forming a solution by dissolving in a solvent
(1) at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof,
(2) at least one tackifying resin, and
(3) at least one scavenger, wherein at least one of the polymer or the tackifying
resin includes at least one impurity, the impurity comprising a compound
with at least one polar reactive moiety;
B. contacting the scavenger with the impurity to form a reaction product;
C. applying the filtered solution to a substrate;
D. drying the solution on the substrate; and
E. applying the substrate to a computer device.
In yet another embodiment, the invention comprises a computer device comprising
at least one component containing a PSA, wherein the PSA comprises:
A. at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof;
B. at least one tackifying resin; and
C. at least one scavenger. As used herein, the tern "styrenic" refers to mono-alkenyl arenes. Thus, a
styrenic polymer or copolymer was formed by the polymerization of at least one mono-
alkenyl arene.
A "block copolymer" was a polymer containing long stretches of two or more
monomeric units linked together by chemical valences in one single chain, such that the
long monomeric stretches alternate with each other in which a block(s) of one type of
polymer structure was attached to a block(s) of another type of polymer structure. A
"diblock copolymer" was a block copolymer that has the general structure A-B, where A
was a long stretch of one homopolymer structure and B was a long stretch of a second
homopolymer structure. A "triblock copolymer" was a block copolymer that has the
general structure A-B-A, where A was a long stretch of one homopolymer structure and B
was a long stretch of a second homopolymer structure.
A "tackifying resin" was a resin that, when added to a rubber or an elastomer, the
resulting composition has the properties of a pressure sensitive adhesive. "Pressure sensitive adhesives" were permanently and aggressively tacky (sticky) solids which form
immediate bonds when two parts were brought together under pressure. For pressure
sensitive adhesives, "tack" can be described as the property whereby the adhesive will
adhere tenaciously to any surface with which it comes into contact under light pressure.
The strength of the bond will be greater under increasing pressure, hence the term
pressure sensitive. Tack can be quantified as the force required to separate an adherend
and an adhesive at the interface shortly after they have been brought rapidly into contact
under a light load of short duration. Tack can be measured by using the ASTM D-2979
procedure. A "scavenger" was a substance added to a system or mixture to consume or
inactivate traces of impurities.
A "hydrocarbon resin" was a resin in the number molecular weight range of a few
hundred up to about 8,000, which was obtained or synthesized from rather basic
hydrocarbonaceous materials such as petroleum, coal, tar, and turpentine.
An improved computer device was prepared by preparing at least one adhesive as
described below and affixing the adhesive to at least one component of the computer
device. Preferably, the component was a film, tape or label which was used to seal or
identify one or more components of the computer device. The computer device was
preferably a disk drive or other data storage device.
The Pressure Sensitive Adhesive
The adhesive used in this invention comprises (i) at least 10, preferably at least 40,
and not in excess of 90, preferably not in excess of 75, weight percent of a polymer, (ii) at
least abut 10, preferably at least 25, and not in excess of 90, preferably not in excess of
60, weight percent of a tackifying resin, and, (iii) at least 0.1 , preferably at least 2, more
preferably at least 3, and not in excess of 8, preferably not in excess of 6, more preferably
not in excess of 4 weight percent of a scavenger, all percentages based on the total weight
of the adhesive.
Polymers
The PSA of this invention comprises polymers typically known in the art of
making PSAs. In general, such polymers impart an elastic or viscoelastic property to the
PSA. Polymers that were useful for the PSAs of this invention include rubbers, such as
natural rubber, and elastomers, such as styrenic-elastomer copolymers, acrylate
copolymers, polyurethanes and combinations thereof. Certain block copolymers have been found useful for making PSAs and, preferably, the polymer of this invention was at
least one hydrogenated block copolymer.
Block copolymers were well-known in the field of PSAs. Any one of these well-
known block copolymers can be included within the composition of this invention,
including those described in some detail within U.S. P. 3,239,478 and 3,917,607. These
particular block copolymers typically take on the general configuration A-B-A or A-B-A-
B, wherein each "A" block, which was generally characterized as an end block, was a
thermoplastic polymer block prepared by a polymerization of a styrenic monomer such as
styrene, a-methyl-styrene, tert-butyl-styrene, and vinyl-toluene.
The elastomer "B" blocks, which were characteristically identified as "mid
blocks," were prepared by the propagation of a polymer chain of a conjugated diene such
as butadiene or isoprene from the end of the end block already synthesized. Then either
using sequential monomer addition or a coupling agent, the desired block copolymers, A-
B-A or A-B-A-B, were generated. If the block copolymers, A-B-A or A-B-A-B were
hydrogenated, a saturated mid block would be obtained. Such block copolymers, which
were prepared by known procedures, include styrene-butadiene-styrene block copolymer
(SBS), styrene-isoprene-styrene block copolymer (SIS), styrene-ethylene butyl ene-styrene
block copolymer (SEBS), styrene-ethylene propylene-styrene (SEPS), anda-
methylstyrene-ethylene propylene-a-methylstyrene. A typical molecular weight for such
block copolymers was between 10,000 and 500,000, expressed as number average
molecular weight.
Preferably, the block copolymer of this invention was a hydrogenated block
copolymer. Hydrogenation minimizes the presence of double bonds in potentially
outgassed materials that could result in those outgassed materials polymerizing on the computer device components. Such polymerization can interfere with the recording,
storage or reading of data in a computer data storage device.
The hydrogenated block copolymer was preferably a block copolymer of
polystyrene and a polydiene, the polydiene typically selected from the group consisting of
polybutadiene and polyisoprene, wherein the unsaturated mid block of either
polybutadiene or polyisoprene was hydrogenated to yield a saturated mid block. The
saturated mid block of the hydrogenated block copolymer has the structure of
poly(ethylene-propylene), poly(ethylene-butylene), or both.
More preferably, the block copolymers of this invention comprise styrene end
blocks and hydrogenated polybutadiene and/or hydrogenated polyisoprene mid blocks.
Such block copolymers were also disclosed in U.S.P. 4, 136,699; 4,361.672; 4,460,364;
4,714,749; and 5,459,193, and in KRATON® Thermoplastic Rubbers published by Shell
Chemical Company.
Most preferably, the block copolymer has end blocks of styrene whose number
average molecular weight was in the range of 10,000 to 30,000, and the mid block was a
block of hydrogenated polyisoprene having a number average molecular weight of
125,000. Such hydrogenated block copolymers were known as styrene-ethylene-
propylene-styrene (SEPS) copolymers. Such block copolymers were commercially
available from the Shell Chemical Company under the trademark KRATON® G.
The KRATON® G hydrogenated block copolymers have a number average
molecular weight (Mn) of 25,000 to 300,000, as measured by gel permeation
chromatography (GPC). Among the KRATON® G polymers, the most preferred were
KRATON® G1650, KRATON® G1652, KRATON® G1654, KRATON® G1657, and KRATON® G1730, or a comb nation thereof. More information on KRATON® G polymers was disclosed in KRATON® Polymers for Adhesives and Sealants, available
from Shell Chemical Company.
In one preferred embodiment of the invention, the block copolymer, in combination with the tackifying resin(s), outgasses less than 1500 ng/cm2 as measured by
Modified IDEMA Ml 1-98 (described later). Optionally, the outgassing content of the
polymer can be reduced by applying removal means to the polymer prior to the
scavenging reaction. Such removal means can comprise extreme high temperature drying,
spray drying, aqueous cleaning, solvent cleaning, or CO, cleaning.
A further embodiment of this invention comprises using a polyurethane as the
polymer. Polyurethanes were thermoplastic polymers produced by the condensation
reaction of a polyisocyanate and a hydroxyl-containing material, e.g., a linear polyester or
polyesters containing hydroxyl groups. The basic polymer unit was formed as shown in
Formula I:
OCNR,NCO + HOR2OH -> -[-CONHR,NHCOOR2O-]n- (I)
where R, and R2 were hydrocarbon radicals or substituted hydrocarbon radicals. Such
polymers were discussed in U.S. P. 4,661,542. An example of such a polyurethane was
ESTANE® 5703 which was commercially available from BF Goodrich.
Natural rubber was a well-known material. Natural rubber was a polyisoprene
derived from latex obtained from Hevea trees, coagulated with acetic or formic acid.
Natural rubber can also be made synthetically. Acrylate copolymers were known in the art. Such acrylic adhesives were discussed in U.S.P. 5,981,666.
Tackifying Resins
Tackifying resins of this invention were resins that associate predominantly with
the elastomeric block or mid block and were substantially incompatible with
nonelastomeric or end blocks. These mid block associating resins were compatible with
the mid block in that between 100 and 200 or more parts by weight of the mid block
associating resin show a clear film when the particular mid block associating resin was
combined with 100 parts of the mid block of the block copolymer and cast from solution in toluene.
In one embodiment of this invention, the tackifying resins usable in this invention,
in combination with the block copolymer(s), outgasses less than 1500 ng/cm2 as measured
by Modified IDEMA Ml 1-98 (described later). Optionally, the outgassing content of the
tackifying resins can be reduced by applying removal means to the tackifying resins prior
to the scavenging reaction. Such removal means can comprise extreme high temperature
drying, spray drying, aqueous cleaning, solvent cleaning, or CO, cleaning.
Examples of tackifying resins that may be useful in this invention include
polyhydric esters of rosin or hydrogenated rosin esters, such as glycerol and
pentaerythritol esters of hydrogenated rosins and of highly stabilized rosins, esters of
polyhydric alcohol, synthetic polyterpenes, terpene-olefin copolymers, terpene-phenols,
tall oil rosin, synthetic saturated hydrocarbon resins, such as saturated alicyclic
hydrocarbons, olefinic resins, aromatic containing resins, phenol-aldehyde resins, a-
pinene resins, a-pinene resins, terpene-phenolic resins, and copolymers such as of 1 ,3-
pentadiene and 2-methyl-2-butene, or mixtures thereof. Other examples of tackifying resins were disclosed in U.S.P. 4,361 ,663 and 4,399,249, and in U.S.P. 4,136,699; 4,361 ,672; 4,714,749; and 5,459,193.
The preferred tackifying resin of this invention was of the type known as
"hydrocarbon resins". A good description of hydrocarbon resins can be found in Kirk-
Othmer, Encyclopedia of Chemical Technology, Second Edition, Vol. 1 1, Interscience,
New York, 1966, pg. 242. Many of the so-called hydrocarbon resins commercially
available today were teφene resins, i.e., polymers with (repeating) isoprene (C5H8) or
C]0H|6 units. These polymers can be natural or synthetic and can be copolymers
(including terpolymers, etc.), since isoprene was an olefin which can be copolymerized
with other olefins. Teφene-phenols were also produced.
Aromatic monomers useful in forming the aromatic containing resin compositions
of this invention can be prepared from any monomer containing substantial aromatic
qualities and a polymerizable unsaturated group. Typical examples of such aromatic
monomers include: styrenic monomers, e.g., styrene, a-methylstyrene, vinyl toluene,
methoxy styrene, tertiary butyl styrene, chlorostyrene, etc.; indene monomers including
indene, methyl indene and others. Aliphatic monomers were typically natural and
synthetic teφenes which contain C6 and C5 cyclohexyl or cyclopentyl saturated groups
that can additionally contain a variety of substantial aromatic ring substituents.
Aliphatic tackifying resins can be made by polymerizing a feed stream containing
sufficient aliphatic monomers such that the resulting resin exhibits aliphatic
characteristics. Such feed streams can contain other aliphatic unsaturated monomers such
as 1 ,3-butadiene, cis-l ,3-pentadiene, trans- 1,3-pentadiene, 2 -methyl- 1 ,3-butadiene, 2-
methyl-2-butene, cyclopentadiene, dicyclopentadiene, teφene monomer, teφene phenolic
resins and others. Mixed aliphatic aromatic resins contain sufficient aromatic monomers and sufficient aliphatic monomers to produce a resin having both aliphatic and aromatic
character. The article by Davis, "The Chemistry of Resins," discusses synthetic C5
resin technology. The preferred tackifying agents were hydrogenated to C,2 resins,
preferably a C9 resin.
Representative examples of useful aliphatic resins include hydrogenated synthetic
C9 resins, synthetic branched and unbranched C5 resins and mixtures thereof.
Representative examples of aromatic tackifying resins include styrenated teφene resins,
styrenated C5 resins or mixtures thereof.
Preferably, the tackifying resin was derived by the polymerization and
hydrogenation of pure monomer hydrocarbon feed stocks (wherein the hydrocarbon
monomer has 5 or 9 carbon atoms). Such hydrocarbon resins were highly stable, light
colored, low molecular weight, non-polar resins and were suggested for use in plastics,
adhesives, coatings, sealants and caulks. Hydrogenation minimizes the presence of
double or triple bonds in potentially outgassed materials that could result in those
outgassed materials polymerizing on the computer device components. Such
polymerization can interfere with the recording, storage or reading of data in a computer
data storage device.
More preferably, the tackifying resin of this invention was low molecular weight
nonpolar hydrocarbon resin commercially available under the trademark REGALREZ®
from Hercules Incoφorated. Most preferably, the tackifying resin was at least one of
REGALREZ® 1018, REGALREZ® 1085, REGALREZ® 1094 and REGALREZ® 1 126. Scavengers
In an electronic assembly, pure hydrocarbons may be tolerated to a relatively higher level than that of the chemicals containing reactive moieties, such as acid, alcohol
or amine, which were undesirable, if not outright unacceptable, even at relatively low
levels. Some of these chemicals containing reactive moieties can be substantially
removed from film-type polymers or formulated adhesives by appropriate drying
conditions. However, chemicals containing reactive moieties may not be fully removed
during drying, especially as the thickness of the adhesive was increased. These chemicals
may then slowly escape from the adhesive to become microcontaminants in a computer
device.
This invention reduces the level of these chemicals that was outgassed, from a
polymer or an adhesive composition, through an "anchoring reaction". The anchoring
reaction was a reaction between reactive groups on the scavengers and reactive moieties
on the outgassing chemicals. The products of these anchoring reactions were either less
susceptible to outgassing, or were less reactive if they do outgas, or both. In this
invention, the anchoring reaction was typically conducted in a solution prepared by
dissolving or suspending the PSA components in a suitable liquid, such as, e.g., toluene.
While the anchoring reaction was normally substantially completed in the solution phase,
it was also possible for trace levels of scavengers to continue reacting at the elevated
temperatures that occur during drying.
The scavengers of this invention react with impurities, such as acids, amines
and/or alcohol, at moderate temperatures, preferably room temperature, and for short time
periods. The products resulting from this achoring reaction must be non- volatile even at elevated temperatures such as 85 °C. The scavengers must be compatible with the PSA system.
Typical scavengers of this invention were low molecular weight compounds and
oligomers that contain groups that react with the reactive moieties of the impurities or
have the ability to absorb chemical impurities. The scavengers used in this invention
were typically chosen based on the impurities present in the adhesive composition or
constituents of the adhesive. Mixtures of scavengers can provide for the capture of
multiple impurities.
Preferably, the scavengers of this invention have moieties that react with the polar
reactive moieties (such as acid, alcohol, amine, etc.) present in typical outgassed materials
found in PSAs. Examples of scavengers usable in this invention include polyisocyanates,
aziridines, aluminum oxide (Al2O3), metallic hydrides, monohydrogen suicides, and
mixtures thereof. Preferred scavengers were polyisocyanates and aluminum oxide.
Suitable polyisocyanates include the DESMONDUR™ series polymers
commercially available from Mobay Coφoration, preferably, DESMONDUR™ 3300 and
DESMONDUR™ 3390. DESMONDUR™ 3300 and DESMONDUR™ 3390 have the
preferred characterisitics of relatively high isocyanate content and low free monomers
content.
The PSA of this invention was conveniently prepared by adding at least 0.1 ,
preferably at least 2, more preferably at least 3, up to 8, preferably not to exceed 6, more
preferably not to exceed 4 weight percent, based on the weight of the total PSA, of the
scavenger(s) to an adhesive system, stirring for a period of time, filtering or decanting the
adhesive when necessary, coating the PSA solution onto a substrate, then drying properly.
Typically, a filtering or decanting step was only needed to remove the anchoring reaction
products formed when aluminum oxide or similar absorbent was used as a scavenger. Optional Components
The PSA's of this invention can optionally include other components known in the
art. These components can include plasticizing oils, resin modifiers, and antioxidants.
A "plasticizing oil", also known as an extending oil, was an organic compound
added to a high polymer both to facilitate processing and to increase the flexibility and
toughness of the final product by internal modification (solvation) of the polymer
molecule. The latter was held together by secondary valence bonds; the plasticizing oil
replaces some of these with plasticizing oil-to-polymer bonds, thus aiding movement of
the polymer chain segments. Among the more important plasticizing oils were
nonvolatile organic liquids and low-melting solids, e.g., phthalate, adipate, and sebacate
esters, polyols, such as ethylene glycol and its derivatives, tricresyl phosphate, castor oil,
etc.
These optional components tend to be "dirty" in that they contain undesirable ions
and/or contribute to outgassing from the PSA. Antioxidants in particular can be harmful
if outgassed into a disk drive system. Therefore, the current preferred embodiments of the
invention do not include these optional components. However, the invention
contemplates use of these ingredients at levels wherein the PSA containing these
ingredients outgasses less than 1500 ng/cm2 as measured by Modified IDEMA Ml 1-98
(described later).
Method of Forming the PSA
The PSA compositions of hydrogenated block copolymers and tackifying resins
can be formed by technologies well known in the art, such as the technologies disclosed
in U.S.P. 4,361,672. Examples of suitable methods for forming PSA's include, inter alia:
(i) compounding on a hot two-roll mill; (ii) melting the block copolymer and the
tackifying resin and mixing the melted components until homogeneous; (iii) other
methods employed in the plastic and elastomer industries, such as high shear intensive
mixing, twin screw extrusion or tandem extrusion techniques; and (iv) dissolving the
mixtures in suitable organic solvents such as toluene and heptane, taking care to form
homogeneous solutions that were then coated on a substrate (e.g., on a film backing)
before the solvent was evaporated.
Hot-melt compounding (any of methods i-iii, above) was not a favored
embodiment of this invention. The heat from these methods can degrade the components
of the PSA, thereby creating more material that can potentially outgas from the PSA.
However, the invention contemplates use of these methods provided that the resulting
PSA outgasses less than 1500 ng/cm2 as measured by Modified IDEMA M l 1 -98.
Preferably, the PSA of this invention was formed by dissolving the mixtures in
suitable organic solvents taking care to form homogeneous solutions that were then
coated on the component for the computer device before the solvent was evaporated.
Preferably, these solutions contain at least 10, more preferably at least 20, most preferably
at least 30, up to preferably 80, more preferably not in excess of 60, most preferably not in
excess of 50, weight percent solids based on the total weight of the solution.
Suitable organic solvents must be inert to the block copolymer and the tackifying
resin. Additionally, the organic solvent must be selected such that substantially all of the solvent can be evaporated from the PSA. "Substantially all of the solvent" refers to removal of the solvent such that the residual levels of solvent were less than 5 percent,
preferably less than 2 percent of the total outgassed materials per Modified IDEMA Ml 1-
98. Preferred organic solvents include toluene, cyclohexane and heptane, more preferably
toluene.
Optionally, the solution can be filtered or decanted after the scavenging reaction
has been accomplished. This option was preferred when aluminum oxide or similar
absorbent was used as a scavenger.
The solvent can be evaporated from the PSA by any technique known in the art,
such as vacuum drying or, preferably, exposure to hot air in a drying oven. The
temperature of the hot air must be maintained below the autoignition point of the solvent.
The appropriate drying conditions were dependent on the substrate to which the PSA was
applied and the process time available for drying. For example, when using a substrate
comprising a Type S polyester film (available from Du Pont), the preferred hot air
temperature for evaporating toluene from the PSA of this invention was 250 °F to 350 °F
for a drying time of 2 to 3 minutes. The practical upper limit on drying time was
deteπnined from the available equipment and the desired production rate.
In one preferred embodiment the PSA was formed by:
A. forming a solution by dissolving in a solvent
(1) at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof, preferably the polymer was at least one of a
hydrogenated styrene-elastomer-styrene block copolymer or a
hydrogenated styrene-elastomer-styrene-elastomer block copolymer, (2) at least one tackifying resin, and
(3) at least one scavenger, wherein at least one of the polymer or the tackifying resin includes at least one impurity, the impurity comprising a compound
with at least one reactive moiety;
B. contacting the scavenger with the impurity to form a reaction product;
C. removing the reaction product from the solution, when necessary;
D. applying the solution to a substrate;
E. drying the solution on the substrate; and
F. applying the substrate to a computer device.
In another preferred embodiment, the substrate of the steps D and E, above, was a
component of a computer device, more preferably, a component of a computer data
storage device.
A hallmark of the PSA of this invention was that the PSA with a scavenger has
lower outgassing, especially of chemicals harmful to a disk drive, than the same adhesive
without a scavenger produced under the same drying temperature and time.
The following specific examples will more precisely describe the invention and
teach the procedures presently preferred in practicing the same, as well as the
improvements and advantages realized thereby. These examples were provided for
illustration puφoses only and shall not be construed to limit the scope of the subject
matter of the invention.
EXAMPLES
Example 1 - Measurement of Outgassed Materials Outgassed materials were measured using the IDEMA Ml 1-98 Dynamic
Headspace Outgas Procedure with the following method details or exceptions (Modified
IDEMA Ml 1-98).
The permanent and expendable equipment (Section 2) consists of a: (a) Type 303
stainless steel cylindrical chamber with approximate internal dimensions: 1.25 inches
deep by 2.25 inches in diameter; (b) Supelco' stainless steel thermal desoφtion tubes
packed with the following sorbent: bed A= 100 milligrams Tenax TA, bed B= 250
milligrams Carbotrap B; (c) Hewlett-Packard2 6890 Gas Chromatograph/ 5973 Mass
Spectrometer; (d) Perkin Elmer3 ATD-400 Automated Thermal Desoφtion Unit; (e)
Reztek4 XTf -5 gas chromatograph column, Reztek pn# 12223; and, n-hexadecane
(Fisher Scientific5 pn# 03035) in dichloromethane employed as external standard for
semi-quantitation.
The sample collection and analysis (Section 3) was conducted as follows. The
thermal desoφtion tubes were conditioned at 320 °C for 8 minutes. Desoφtion tubes were installed and the samples were placed in the sample outgassing chambers. The
sample chamber flow rate was set at approximately 50 milliliters per minute (ml/min.)
using 99.99 percent nitrogen gas. The outgassing chamber was continuously heated at 85
°C. The desorber was programmed to desorb at 320 °C for 8 minutes at 50 ml/min. The
cold trap was set at -30 °C and desorbed at 350 °C, with a hold time of 8 minutes, and
valve and line temperatures set at 200°C. The outlet split was set at 54 ml/min. The
sample split ratio was approximately 49: 1. The gas chromatograph flow rate was
approximately 1 ml/min.
Semi-quantitation was accomplished by injecting 5 microliters of a 200 nanogram
per microliter dichloromethane solution of n-hexadecane into a heated sample chamber via an in-line injection port and outgassing onto reconditioned thermal desoφtion tubes for 185 minutes at 85 °C. The response factor was calculated by averaging the peak area
of the total ion chromatogram for at least 6 replicates.
The amount of target compound or compounds was calculated (Section 4) by
dividing the total ion count for the peak of the target compound or compounds by the
external standard response factor and multiplying by 1 ,000 nanograms. The total
outgassing for the sample was determined by integrating the top 20 ± 2 peaks. The final
result was expressed as nanograms per square centimeter where the sample area was
determined by summing the area of both sides of a film sample.
Notes
( 1 ) Supelco, Supelco Park, Bellefonte, PA 16823-0048 USA.
(2) Hewlett-Packard Company, Chemical Analysis Group, 2850 Centerville Road, Wilmington, DE 19808-1610 USA.
(3) The Perkin-Elmer Coφoration, 761 Main Avenue, Norwalk, CT 06859- 0010 USA.
(4) Reztek Coφoration, 1 10 Benner Circle, Bellfonte, PA 16823 USA.
(5) Fisher Scientific, 71 1 Forbes Avenue, Pittsburgh, PA 15219-4785 USA
Example 2 - Block Copolymer PSA Examples
A Comparative Sample (A) and three examples of the PSA of the invention (B, C,
D) were prepared by dissolving the components in toluene to form a 35.5 percent solids
solution. The formulas for each of these examples were shown in TABLE 1. None of the
adhesive solutions of B, C or D were filtered or decanted.
TABLE 1 - Block Copolymer PSA Formulas
Figure imgf000022_0001
* SEBS - polystyrene-(polyethylene-butylene)-polystyrene
** SEPSEP - polystyrene-(polyethylene-propylene)-polystyrene-(polyethylene-propylene)
3 weight percent based on total composition weight
4 weight percent based on total composition weight
MORESTER 49007 is a registered trademark owned by Morton international which was added as a modifier but has no eftect on the final properties of the adhesive
Each adhesive solution was coated onto a separate polyester film and dπed at 300
°F for 3 minutes The dπed adhesive films were 1 mil thick Then the coated polyester
film was die-cut into the same size specimens and their outgassing was tested using a gas
chromatograph-mass spectrometer according to Modified IDEMA Ml 1-98. The results
of the outgassing measurements were shown in TABLE 2 These results demonstrate that
the use of a scavenger substantially decreases, by at least 16 percent, the amount of
outgassed mateπal in a PSA compπsing hydrogenated block copolymers TABLE 2 - Outgassing Results for Block Copolymer PSAs
Figure imgf000023_0001
Example 3 - Polyurethane PSA Examples
This example demonstrates the reduction of outgassed material in a polyurethane
which can then be used to prepare a PSA. A high level of butylated hydroxytoluene
(BHT) was measurable in ESTANE® 5703 (a polyurethane available from BF Goodrich)
as shown in TABLE 3. A comparative example (E) was prepared by dissolving
ESTANE® 5703 in dioxolane to form a 10 percent solution. An example of the invention
(F) was prepared by making a solution containing 10 percent ESTANE® 5703, 0.5
percent of Al2O3 and 89.5 percent of dioxolane, all percentages were by weight based on
the total weight of the solution. Both Comparative Example E and Example F were
stirred for 24 hours at room temperature. The Al,O3 and the product of the scavenging
reactions formed a precipitate from which the polymer solution was decanted. These
solutions were carefully coated onto separate pieces of TESLIN™ paper (a porous
polyproplene film available from DuPont). Preferably, the solution was uniformly
absorbed into the paper. The coated paper samples were then dried at room temperature
until no weight change was detected after 1 hour. The outgassing was measured
according to Modified IDEMA Ml 1-98 and the results were shown in TABLE 3. These results demonstrate that the use of a scavenger of this invention also decreases outgassing
in polyurethanes by at least 30 percent.
TABLE 3 - Outgassing Results for Polyurethane
Figure imgf000024_0001
ESTANE® is a trademark of BF Goodrich.

Claims

WHAT IS CLAIMED IS:
1. An improved pressure sensitive adhesive (PSA) comprising:
A. at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof;
B. at least one tackifying resin; and
C. at least one scavenger.
2. The PSA of Claim 1 wherein the polymer comprises at least one of a hydrogenated
styrene-elastomer-styrene block copolymer or a hydrogenated styrene-elastomer-
styrene-elastomer block copolymer.
3. The PSA of Claim 1 wherein the scavenger was selected from the group
consisting of polyisocyanates, aziridines, aluminum oxide, metallic hydrides,
monohydrogen suicides, and mixtures thereof.
4. The PSA of Claim 1 in which the PSA outgasses less than 1500 ng/cm2 as
measured by Modified IDEMA M 1 1 -98.
5. The PSA of Claim 1 in which the PSA outgasses less than 500 ng/cm2 as
measured by Modified IDEMA Ml 1 -98.
6. The PSA of Claim 1 in which the PSA outgasses at least 16 percent less material,
as measured by Modified IDEMA Ml 1 -98, than a similar PSA, without a
scavenger.
7. The PSA of Claim 2 in which the PSA outgasses at least 16 percent less material,
as measured by Modified IDEMA Ml 1-98, than a similar PSA, without a
scavenger.
8. The PSA of Claim 2 in which the elastomer component of the hydrogenated
styrene-elastomer-styrene block copolymer or the hydrogenated styrene-elastomer- styrene-elastomer block copolymer was composed of poly(ethylene-propylene) or
poly(ethylene-butene) or both.
9. The PSA of Claim 2 in which the elastomer component of the hydrogenated
styrene-elastomer-styrene block copolymer or the hydrogenated styrene-elastomer- styrene-elastomer block copolymer was made by the polymerization of one or
more of (i) isoprene, or (ii) 1,3-butadiene.
10. The PSA of Claim 2 in which the PSA comprises between 10 to 90 weight percent
of the block copolymer, between 10 to 90 weight percent of the tackifying resin,
and between 0.1 to 10 weight percent of the scavenger, based on the weight of the
PSA.
1 1. The PSA of Claim 1 in which the tackifying resin was a hydrocarbon resin.
12. The PSA of Claim 1 1 in which the tackifying resin was hydrogenated.
13. An improved method for preparing a computer device which includes at least one
component bearing a PSA, the method comprising the steps of:
A. forming a solution by dissolving in a solvent
(1) at least one polymer selected from the group consisting of natural
rubber, styrenic-elastomer copolymers, acrylate copolymers,
polyurethanes and combinations thereof,
(2) at least one tackifying resin, and
(3) at least one scavenger, wherein at least one of the polymer or the
tackifying resin includes at least one impurity, the impurity
comprising a compound with at least one reactive moiety; B. contacting the scavenger with the impurity to form a reaction product;
C. applying the solution to a substrate;
D. drying the solution on the substrate; and
F. applying the substrate to a computer device.
14. The method of Claim 13 wherein the polymer was a hydrogenated styrene-
elastomer-styrene block copolymer or a hydrogenated styrene-elastomer-styrene-
elastomer block copolymer.
15. The PSA of Claim 13 wherein the scavenger was selected from the group
consisting of polyisocyanates, aziridines, aluminum oxide, metallic hydrides,
monohydrogen silicides, and mixtures thereof.
16. The method of Claim 13 further comprising the step of separating the reaction
product from the solution prior to applying the solution to the substrate.
17. The method of Claim 13 in which the computer device was a data storage device.
18. The method of Claim 13 wherein the PSA outgasses less than 1500 ng/cm2 as
measured by Modified IDEMA M 1 1 -98.
19. The method of Claim 13 in which the PSA outgasses at least 16 percent less
material, as measured by Modified IDEMA 1 1 -98, than a second PSA of the
same composition except that the second PSA does not comprise a scavenger.
20. A computer device comprising at least one component containing a PSA, wherein
the PSA comprises:
A. at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof; B. at least one tackifying resin; and
C. at least one scavenger.
21. The computer device of Claim 20 wherein the polymer comprises at least one of a
hydrogenated styrene-elastomer-styrene block copolymer or a hydrogenated
styrene-elastomer-styrene-elastomer block copolymer.
22. The computer device of Claim 20 in which the computer device was a computer
data storage device.
23. The computer device of Claim 20 wherein the scavenger was selected from the
group consisting of polyisocyanates, aziridines, aluminum oxide (Al2O3), metallic
hydrides, monohydrogen suicides, and mixtures thereof.
24. The computer device of Claim 20 wherein the PSA outgasses less than 1500
ng/cm2 as measured by Modified IDEMA Ml 1-98.
25. The computer device of Claim 20 in which the PSA outgasses at least 16 percent
less material, as measured by Modified IDEMA M l 1-98, than a second PSA of
the same composition except that the second PSA does not comprise a scavenger.
26. The computer device of Claim 21 in which the PSA outgasses at least 16 percent
less material, as measured by Modified IDEMA Ml 1 -98, than a second PSA of
the same composition except that the second PSA does not comprise a scavenger.
27. An improved PSA consisting essentially of:
A. at least one polymer selected from the group consisting of natural rubber,
styrenic-elastomer copolymers, acrylate copolymers, polyurethanes and
combinations thereof;
B. at least one tackifying resin; and
C. at least one scavenger.
8. The PSA of Claim 27 wherein the polymer comprises at least one of a hydrogenated styrene-elastomer-styrene block copolymer or a hydrogenated
styrene-elastomer-styrene-elastomer block copolymer.
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