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the coagulation of the aqueous polymer latexresultingupon the emulsion polymerization
polymer scale deposition ... difficultto prevent ... e.g., ... , in emulsion polymerization
sample B. A control rubber compositioncomposedof emulsion polymerization
Blending of PVDF latex ,resulting directlyfrom emulsion polymerization
those latexesresultingfrom emulsion polymerization
Samples A , B and C. A control rubber compositioncomposedof emulsion polymerization
The Example 2 polymer produced using AerosolresultedA-102 in the emulsion polymerization
the seed latexresultingfrom emulsion polymerization
because such a monomer is dissolved in the aqueous suspensionto causeemulsion polymerization
a hydrophilic functional group such as an amino group , a carboxylic group , a hydroxyl group , a sulfonic acid group , a glycidyl group or a nitrile group , which can not be used because it is water - soluble as a monomer and hence dissolves in an aqueous suspensionto causeemulsion polymerization
a polymerizable monomer unit containing a hydrophilic functional group such as an amino group , a carboxylic group , a hydroxyl group , a sulfonic acid group , a glycidyl group or a nitrile group ... because it is water - soluble and dissolves in an aqueous suspensionto causeemulsion polymerization
a polymerizable monomer component containing a hydrophilic functional group such as an amino group , a carboxylic acid group , a hydroxyl group , a sulfonic acid group , a glycidyl group or a nitrile group ... because it is water - soluble and dissolves in an aqueous suspensionto causeemulsion polymerization
a basic three elastomerscomposedof emulsion polymerization
good heat exchange conditions and thus by the opportunity of keeping of necessary temperature conditions in all points of a system , as well as the opportunity of adding various additives which influence the polymer qualities during polymerization(passive) is caused byEmulsion polymerization
The very transparent , bluish - white dispersionresultingfrom the emulsion polymerization
a hydrophilic functional group such as an amino group , a carboxylic acid group , a hydroxyl group , a sulfonic acid group , a glycidyl group or a nitrile group , which can not be used because it is water - soluble and hence dissolve in an aqueous suspensionto causeemulsion polymerization
the emulsionsresultingfrom emulsion polymerization
an emulsifying capability good enoughto causeemulsion polymerization
fluoroelastomersresultingfrom emulsion polymerization
free radicalscontributeto emulsion polymerization
10 grams of polyoxyethylenenonylphenyl ether ( 70 percent active ) , and 4 grams of potassium iodide were addedto preventemulsion polymerization
the acrylic PSA dispersionsresultingfrom emulsion polymerization
the inventive polymeric productresultingfrom emulsion polymerization
Proper choice of dispersants is conditioned by two factors : ( 1 ) ability to prevent agglomeration or gelation of the polymerizing mass ; and ( 2 ) a necessary lack of emulsification of the water released in dehydration of the decahydrateto preventemulsion polymerization of acrylamide
a hydrolyzable fluoropolymerresultingfrom emulsion polymerization
a core - shell structureresultingfrom emulsion polymerization
the copolymer productresultingfrom the emulsion polymerization
initiation and polymerization in the aqueous phase ... to be avoidedto preventemulsion polymerization
smaller droplet sizesleadto emulsion polymerization
using water - soluble initiators(passive) can be triggeredThe emulsion polymerization
amounts sufiicientto preventpolymerization of the emulsion
its water - solubilityto causeemulsion polymerization
water - based suspensionscausingemulsion polymerization
2 parts were continuously titrated into the reaction tank in 30 minutes by means of respective separate titration funnelto causeemulsion polymerization
such particle sizes ( number average diameterresultfrom an emulsion polymerization
such particle sizes ( Z average particle diameterresultfrom an emulsion polymerization
10 parts were continuously titrated into the reaction tank in 2 hours by means of respective separate titration funnelto causeemulsion polymerization
the copolymer emulsionresultingfrom emulsion polymerization
the materialscausingthe undesired emulsion polymerization
a free radical initiator(passive) is typically triggered byThe emulsion polymerization
to materials easily processed ... either by film casting techniques ( water evaporation for paint applications for example ) or by freeze - drying ( or more simply by flocculation ... followed by classical extrusion processcan leadto materials easily processed ... either by film casting techniques ( water evaporation for paint applications for example ) or by freeze - drying ( or more simply by flocculation ... followed by classical extrusion process
in a high stability product with a fine particle sizeresultingin a high stability product with a fine particle size
in nano size molecularly - imprinted polymer ( MIP ... with narrow size distribution whereas bulk polymerisation resulted in irregular shaped micron size particlesresultedin nano size molecularly - imprinted polymer ( MIP ... with narrow size distribution whereas bulk polymerisation resulted in irregular shaped micron size particles
in an aqueous latex emulsionresultingin an aqueous latex emulsion
in a novel lignin based latexresultingin a novel lignin based latex
in average emulsion particle size of 32 nanometers ( particle size estimated using light scattering methodsresultingin average emulsion particle size of 32 nanometers ( particle size estimated using light scattering methods
in polymer particles of small sizescan resultin polymer particles of small sizes
Magnetic particles of this size range(passive) can be created byMagnetic particles of this size range
in substantially spherical particles of about 10 nmresultsin substantially spherical particles of about 10 nm
solid particles dispersed in an aqueous medium and an additiveto createsolid particles dispersed in an aqueous medium and an additive
in the formation of fine particles having a diameter of not more than 1 μmresultingin the formation of fine particles having a diameter of not more than 1 μm
in a series of particles having extremely uniform size distributionsresultsin a series of particles having extremely uniform size distributions
to the production of a fine dispersion of polymer particles in a continuous aqueous mediumleadsto the production of a fine dispersion of polymer particles in a continuous aqueous medium
solid particles dispersed in an aqueous medium and an ... US-1,005,3594 Microgelsto createsolid particles dispersed in an aqueous medium and an ... US-1,005,3594 Microgels
to particles of especially appropriate size ( in the nanometer range ... and with other advantageous properties , such as ( semi- ) transparency in dispersionleadsto particles of especially appropriate size ( in the nanometer range ... and with other advantageous properties , such as ( semi- ) transparency in dispersion
the formation of fine particles having a particle diameter distribution such that most of the particles have a particle diameter of not more than 1 μm and thus is not appropriate for the preparation of the particulate resin of the present inventioncausesthe formation of fine particles having a particle diameter distribution such that most of the particles have a particle diameter of not more than 1 μm and thus is not appropriate for the preparation of the particulate resin of the present invention
formation of microsuspension polymer particles and to ensure a homogeneous concentration of reagents to produce a stable emulsion with consistent properties that are more desirable for aggregation / coalescence processes than the properties of similar latexes prepared without pre - emulsificationto preventformation of microsuspension polymer particles and to ensure a homogeneous concentration of reagents to produce a stable emulsion with consistent properties that are more desirable for aggregation / coalescence processes than the properties of similar latexes prepared without pre - emulsification
to coagulate or agglomerate to form larger particles when subjected to purification procedures ... and which contain contaminants in the aqueous...http://www.google.com/patents/US3944513?utm_source=gb-gplus-sharePatent US3944513 - Purification of polymer dispersions with adsorbent carbon particlesAdvanced Patent SearchPublication numberUS3944513 APublication typeGrantApplication numberUSmay be causedto coagulate or agglomerate to form larger particles when subjected to purification procedures ... and which contain contaminants in the aqueous...http://www.google.com/patents/US3944513?utm_source=gb-gplus-sharePatent US3944513 - Purification of polymer dispersions with adsorbent carbon particlesAdvanced Patent SearchPublication numberUS3944513 APublication typeGrantApplication numberUS
to an aqueous colloidal dispersion of the polymerleadsto an aqueous colloidal dispersion of the polymer
to an aqueous dispersion of the polymerleads directlyto an aqueous dispersion of the polymer
of a compound represented by general formula ( Iis composedof a compound represented by general formula ( I
from monomers to a plastic or rubber dispersionleadingfrom monomers to a plastic or rubber dispersion
in a finely divided , stable dispersion of the copolymerresultsin a finely divided , stable dispersion of the copolymer
in the formation of a layer of polyacrylonitrileresultingin the formation of a layer of polyacrylonitrile
in dispersions with good stability over timeresultsin dispersions with good stability over time
in a high stabresultingin a high stab
in the dispersion and in the preparation of secondary polymer dispersionsresulting primarilyin the dispersion and in the preparation of secondary polymer dispersions
to a shape with immobility , water and emulsifierleadsto a shape with immobility , water and emulsifier
to aqueous polymer dispersions which generally have solids contents of from 15 to 75 % by weight , preferably from 40 to 75 % by weightleadsto aqueous polymer dispersions which generally have solids contents of from 15 to 75 % by weight , preferably from 40 to 75 % by weight
in the formation of at least two mutually incompatible polymer compositionscan resultin the formation of at least two mutually incompatible polymer compositions
the resin dispersionto createthe resin dispersion
in fine uniform polymer microparticlescan resultin fine uniform polymer microparticles
in an average emulsion particle size of about 120 nanometersresultingin an average emulsion particle size of about 120 nanometers
alsocan ... influencealso
the resin fine particle surface(passive) created bythe resin fine particle surface
in highly uniform spheres and a high degree of structural and functional homogeneityresultsin highly uniform spheres and a high degree of structural and functional homogeneity
in a soft rubbery horhopolymer which was both hydrophobic and oleophobicresultedin a soft rubbery horhopolymer which was both hydrophobic and oleophobic
in substantially higher polymerization rates than are obtained either in solution polymerization or in bulk polymerizationresultsin substantially higher polymerization rates than are obtained either in solution polymerization or in bulk polymerization
a previously unrecognized polymer construction , which he named “ microgel”—a three - dimensional solitary - polymer macromolecule , of standard size 100 nm , somewhat cross - joined and significantly swollen by solventdesigneda previously unrecognized polymer construction , which he named “ microgel”—a three - dimensional solitary - polymer macromolecule , of standard size 100 nm , somewhat cross - joined and significantly swollen by solvent
to much more improvement in the propertiescausesto much more improvement in the properties