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CH HYPERDISPERSANT STRUCTURE & PRORERTIES SHANGHAI SANZHENG POLYMER MATERIAL Co.,LTD

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  • Slide 1
  • CH HYPERDISPERSANT STRUCTURE & PRORERTIES SHANGHAI SANZHENG POLYMER MATERIAL Co.,LTD
  • Slide 2
  • DISPERSING PROCESS OF PIGMENTS s 1) WETTING L/S INTERFACE--S/G INTERFACE s 2) DEAGGLOMERATION BREAKAGE & REAGGLOMERATION s 3) STABILIZATION REMAINING PARTICLE SIZE & ITS DISTRIBUTION
  • Slide 3
  • MECHANISM OF DISPERSION STABILIZATION s ELECTROSTATIC STABILIZATION DOUBLE--LAYER THEORY s STERIC STABILIZATION OSMOTIC REPULSION THEORY ENTROPIC REPULSION THEORY
  • Slide 4
  • DEEFFICIENCY OF CLASSICAL SURFACTANTS s HYDROPHILIC GROUP NOT DESIGNED FOR PIGMENT SURFACE, EASY TO DESORB s HYDROPHOBIC GROUP NON-POLAR STRUCTURE INCOMPATIBLE WITH POLAR MEDIA 18 CARBON ATOMS, TOO SHORT
  • Slide 5
  • MOLECULAR STRUCTURE OF CH HYPERDISPERSANTS PARTICLE Anchoring Group Solvatable Chain
  • Slide 6
  • ANCHORING GROUP s DESIGNED FOR PIGMENT SURFACE STRONG POLARITY SURFACE SINGLE-SPOT CHEMICAL BONDING WEAK POLARITY SURFACE MULTI-SPOT HYDROGEN BONDING NON-POLAR PIGMENT SURFACE SURFACE SYNERGIST
  • Slide 7
  • SOLVATABLE CHAIN s MONO-FUNCTIONAL TERMINAL s JUSTABLE COMPATIBILITY MONOMER STRUCTURE MONOMER RATIO SOLVATABLE CHAIN POLARITY s LENGTH OF SOLVATABLE CHAIN CONTROLLED MOLECULAR WEIGHT ADEQUATE CHAIN LENGTH
  • Slide 8
  • MORPHOLOGY OF HYPERDISPERSANT STRONG POLARITY SURFACE WEAK POLARITY SURFACE NON-POLAR SURFACE
  • Slide 9
  • ADSORPTION PROPERTIES OF HYPERDISPERSANT Rehacek Method Ca Ce tg=Ma Xap MaCa
  • Slide 10
  • (Mn=700) (Mn=1500) (Mn=700) (Mn=1500)
  • Slide 11
  • RHEOLOGICAL PROPERTIES OF THE DISPERSION WITH HYPERDISPERSANT Viscosity-reducing properties Influence of anchoring group Influence of solvatable chain Viscosity-reducing properties
  • Slide 12
  • STABILIZATION PROPERTIES OF THE DISPERSION WITH HYPERDISPERSANT Deposition curve of magnetic dispersion Viscosity stability of the ink with hyperdispersant
  • Slide 13
  • METHOD OF USE OF HYPERDISPERSANTS s MINIMAL RESIN REDUCED RESIN SOLIDS--LOWERED VISCOSITY & STABILITY s ADDING HYPERDISPERSANT IMPROVED STABILITY FURTHER REDUCED VISCOSITY s IMPROVING PIGMENT CONTENT HIGH PIGMENT / VEHICLE RATIO HIGH STABILITY, NORMAL VISCOSITY
  • Slide 14
  • NOTATION FOR USE OF HYPERDISPERSANT s ADDED BEFORE PIGMENTS, FILLERS AND OTHER INGREDIENTS s ADDING SURFACTANTS DURING LET-DOWN OR LATER STAGES s DOSAGE DEPENDS ON SURFACE AREA(ABOUT 2MG/M2)
  • Slide 15
  • ADVANTAGES OF HYPERDISPERSANTS s FAST WETTING, SHORTER MILLING TIME, IMPROVED PRODUCTIVITY s HIGH PIGMENT / VEHICLE RATIO, LESS ENERGY AND LABOUR COST s REDUCED VISCOSITY, IMPROVED RHEOLOGICAL PROPERTIES s IMPROVED DISPERSING STABILITY, IN AVOID OF RE-DISPERSION
  • Slide 16
  • ADVANTAGES OF HYPERDISPERSANTS s WIDE COMPATIBILITY OF MILLBASE s NOT EASY TO BE OXIDIZED, LESS SURFACE WASTAGE PRODUCED s HYDROPHOBIC DISPERSANTS NO HYDROPILIC FILM INDUCED s COMPLETE WETTING AND BETTER APPLICATION QUALITIES
  • Slide 17
  • CH Hyperdispersant s Counter part Counter part
  • Slide 18
  • HYPERDISPERSANT SELECTION s..\sszl\Echyn.htm..\sszl\Echyn.htm s..\sszl\Echym.htm..\sszl\Echym.htm s..\sszl\Echyq.htm..\sszl\Echyq.htm s..\sszl\Echsl.htm..\sszl\Echsl.htm
  • Slide 19
  • HYPERDISPERSANT OFFSET INK APPLICATION
  • Slide 20
  • BENEFITS l IMPROVED QUALITY HIGHER GLOSS GREATER INTENSITY MORE TRANSPARENCY l HIGHER PRODUCTIVITY SHORTER DISPERSION TIMES HIGHER PIGMENT CONTENT
  • Slide 21
  • BENEFITS l MORE FLEXIBILITY MORE VERSATILE MILLBASE HEATSET AND SHEETFET FROM SAME MILLBASE MORE STABLE CONCENTRATES ABILITY TO TRANSPORT
  • Slide 22
  • HYPERDISPERSANT FOR OFFSET INKS l HYPERDISPERSANT SELECTION FOR LITHOL RUBINE / RUBINE TONER USE CH-5 ONLY FOR PHTHALOCYANINE BLUE OR CARBON BLACK USE CH-5 + CH-11B FOR DIARYLIDE YELLOW USE CH-5 + CH-22
  • Slide 23
  • TYPICAL DOSAGE l (SHOWN AS WEIGHT OF PIGMENT) RUBINE-------8%----CH-5 BLUE---------10%----3:1 CH-5:CH-11B YELLOW---10%---3:1 CH-5:CH-22 BLACK------4%--10% CH-5 (DEPENDS ON THE SPECIAL SURFACE OF CARBON BLACK)
  • Slide 24
  • GUIDELINES FOR USE l REDUCING RESIN SOLID TO 30-40% IN MILLBASE l HOLD BACK IN MILLBASE AS MUCH AS POSSIBLE GELLED VEHICLE OR GELLING AGENT l ADDING HIGHER PROPORTIONS OF GELLED VEHICLE / GELLING AGENT AT THE LET-DOWN STAGE TO COMPENSATE
  • Slide 25
  • TYPICAL FORMULATION HEATSET / SHEETFET MILLBASE
  • Slide 26
  • TYPICAL FORMULATION GRINDING VEHICLE
  • Slide 27
  • TYPICAL FORMULATION LET-DOWN VARNISHES
  • Slide 28
  • TYPICAL FORMULATION FINAL INK FORMULATIONS
  • Slide 29
  • Slide 30
  • CH-35 WATER PICK-UP REDUCING AGENT APPLICATION IN OFFSET PRINTING INK AND FLUSH
  • Slide 31
  • BENEFITS OF CH-35 l REDUCING EMULSIFICATION, IMPROVING THE FLUIDITY, TRANSFERRING AND PRINTING DENSITY OF OFFSET INK l REDUCING WATER PICK-UP, FAST CREATING WATER BALANCE l ACCELERATING THE OUT-COMING OF WATER IN FLUSH l CONVENIENT TO USE
  • Slide 32
  • METHOD OF USE OF CH-35 l ADDED IN THE VEHICLE DURING THE PREPARATION PROCESS OF INK OR FLUSH OR ADDED IN THE INK PRODUCT l COMPLETELY MIXED WITH VEHICLE l AT THE DOSAGE OF 0.2-0.4%
  • Slide 33
  • CH-1 HYPERDISPERSANT APPLICATION IN MASTERBATCH AND PLASTIC COMPOUNDS
  • Slide 34
  • BENIFITS OF CH-1 l REDUCED PIGMENT COST l IMPROVED PRODUCTIVITY l IMPROVED PRODUCT QUALITY l REDUCED MANUFACTURE COST l IMPROVED PROCESSING l NO OBVIOUS ADVERSE EFFECTS
  • Slide 35
  • METHOD OF USE OF CH-1 Charge polymer to high speed blender or tumbler Add CH-1 and blend thoroughly with polymer (2min/1800rpm blender or 5min tumbling) Add pigments, fillers, processing aids and other essential ingredients and continue blending. (1min/1800rpm blending or 15min tumbling) Process resultant blend in normal manner. e.g. extrusion,internal mixing, or 2-roll milling.
  • Slide 36
  • TYPICAL FORMULATION OF CH-1 IN PE MASTERBATCH
  • Slide 37
  • TYPICAL FORMULATION OF CH-1 IN RIGID PVC--WINDOW PROFILE COMPOUND
  • Slide 38
  • TYPICAL FORMULATION OF CH-1 IN PVC BOTTLE COMPOUND
  • Slide 39
  • TYPICAL FORMULATION FLEXIBLE PVC--CABLE l FORMULATION OF TBLS TRIBASIC LEAD SULPHATE 80PHR LEAD 5PHR; DOP 8PHR; SNOWCAL70 5PHR
  • Slide 40
  • TYPICAL FORMULATION OF CH-1 IN ABS
  • Slide 41
  • TYPICAL FORMULATION OF CH-1 IN PS
  • Slide 42
  • CH-2 HYPERDISPERSANT APPLICATION IN PLASTICISER DISPERSION
  • Slide 43
  • CH-2 HYPERDISPERSANT FOR PLASTICISER DISPERSION l BENEFITS LOW VISCOSITY, GOOD FLOW AND PUMPABILITY HIGH PIGMENT CONTENT, IMPROVED PRODUCTIVITY MORE NEWTONIAN RHEOLOGY IMPROVED COLOUR STRENGTH
  • Slide 44
  • CH-2 HYPERDISPERSANT FOR PLASTICISER DISPERSION l BENEFITS SHORTER MILLING TIMES, LOWER ENERGY CONSUMPTION, LOWER LABOUR AND FIXED COSTS LESS COLOUR SEPARATIO WIDE COMPATIBILITY NO ADVERSE EFFECT ON PLASTICS
  • Slide 45
  • METHOD OF USE OF CH-2 l ADDED AND DISSOLVED INTO PLASTICISER BEFORE ADDING OTHER INGREDIENTS l AT DOSAGE OF ABOUT 1--5% OF THE TOTAL WEIGHT OF PIGMENTS AND FILLERS l HIGH PIGMENT LOADING
  • Slide 46
  • TYPICAL FORMULATION OF CH-2 IN PLASTICISER DISPERSION
  • Slide 47
  • APPLICATION IN PLASTICISER DISPERSION CH-6 HYPERDISPERSANT
  • Slide 48
  • CH-6 HYPERDISPERSANT FOR PLASTICISER DISPERSION l BENEFITS LOW VISCOSITY, GOOD FLOW AND PUMPABILITY HIGH PIGMENT CONTENT, IMPROVED PRODUCTIVITY MORE NEWTONIAN RHEOLOGY IMPROVED COLOUR STRENGTH
  • Slide 49
  • CH-6 HYPERDISPERSANT FOR PLASTICISER DISPERSION l BENEFITS SHORTER MILLING TIMES, LOWER ENERGY CONSUMPTION, LOWER LABOUR AND FIXED COSTS LESS COLOUR SEPARATIO WIDE COMPATIBILITY NO ADVERSE EFFECT ON PLASTICS
  • Slide 50
  • METHOD OF USE OF CH-6 l ADDED AND DISSOLVED INTO PLASTICISER BEFORE ADDING OTHER INGREDIENTS l AT DOSAGE OF ABOUT 5-15% OF THE TOTAL WEIGHT OF CARBON BLACK OR ORGANIC PIGMENTS l HIGH PIGMENT LOADING
  • Slide 51
  • TYPICAL FORMULATION
  • Slide 52
  • CH-4 HYPERDISPERSANT APPLICATION IN SURFACE TREATMENT
  • Slide 53
  • BENEFITS OF CH-4 l MAKE PIGMENT HYDROPHOBIC LESS WATER CONTENT EASY TO BE FILTERED AND DRIED l MAKE PIGMENT AGGEARATED LOOSELY EASY TO BE DISPERSED l REDUCED OIL ADSORPTION IMPROVED HEAT STABILITY AND COLOUR STRENGTH
  • Slide 54
  • METHOD OF USE OF CH-4 l ADDED AND MIXED COMPLETELY WITH PIGMENT OR FILLER AT ANY STAGE BEFORE FILTERING PROCESS l DOSAGE ABOUT 10-50% OF THE DRY WEIGHT OF PIGMENTS