mitsui plastics inc. - spe...polyolefins g-cat/xxxxg polyolefin ppm ti in polyolefin phenolic ao ppm...

41
Mitsui Plastics Inc. New Catalyst Neutralizer Polymer Protector Additive for Polyethylene Presented to the 2019 SPE Polyolefins Conference, Houston, TX Feb 24-27, 2019 Mitsui Plastics Inc. presentation to SPE Polyolefins Conference 1

Upload: others

Post on 23-Oct-2020

5 views

Category:

Documents


0 download

TRANSCRIPT

  • Mitsui Plastics Inc.

    New Catalyst Neutralizer Polymer

    Protector Additive for Polyethylene

    Presented to the 2019 SPE Polyolefins Conference, Houston, TX

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    1

  • History of acid scavengers in

    Polyolefins:

    First Generation 1955 + : For over 60 years Metallic Stearates and

    oxides have been used in PE. Originally designed for 1-3rd

    generation non-magnesium supported. Poor polyolefin oxidative

    stability requiring higher AO levels. Lewis Acid problem.

    Second Generation 1984+; Hydrotalcite used in PP and solution

    process LLDPE only. Improved oxidative stability. Color issues with

    certain catalysts and AO’s from high pH.

    Third Generation 2017+; Mitsui M-Series catalyst neutralizers and

    polymer protectors for 4th -6th generation catalysts. Lower color

    improved and highest oxidative stability allowing AO reduction.

    JAN 2018MPI Confidential Developmental ZRx Series

    2

  • Mitsui M-Series Catalyst Neutralizer

    Chemistry comparisons

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    3

    Mitsui Plastics Inc. Metallic Stearates,

    OxidesVarious CAS numbers FDA EU 10/2011 listed

    Additive number: 3L 7L 37L 70P, 737LP CaSt, ZnSt, ZnO

    North America Supply Developmental quantities

    Developmental quantities

    Developmental quantities

    Developmental quantities

    USA, EU, Asia

    Particle size range in microns 0.5-0.8 0.5-0.8 0.5-0.8 0.5-0.8 10-35

    Stoichiometry Formulation

    Trade Secret Trade Secret Trade Secret Trade Secret (C17H35COO)2 Ca(C17H35COO)2 Zn

    ZnO

    Acid mechanism:

    Catalyst design:

    Catalyst Neutralizer

    Polymer protector

    4th , 5th 6th generation

    Catalyst Neutralizer

    Polymer protector

    4th , 5th 6th generation

    Catalyst Neutralizer

    Polymer protector

    4th , 5th 6th generation

    Catalyst Neutralizer

    Polymer protector

    4th , 5th 6th generation

    Acid Scavenger

    1st and 2nd

    generaton

  • Mitsui Plasticscatalyst neutralizer efficiency

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    4

  • Catalyst acid neutralizer efficiency

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    5

    0 500 1000 1500 2000 2500

    1

    2

    3

    4

    5

    6

    7

    8

    Neutralizer increasing efficiency

    Acid HCL ppm from TiCL4-MgCl2 Neutralizer ppm

    36.1 average efficiency 500 ppm to neutralize 35 ppm of acid

    4.8:1 average efficiency 1000 ppm to neutralize 210 ppm of acid

    10:1 average efficiency : 700 ppm to

    neutralize 70 ppm acid

    3.4:1

    Catalyst Efficiency

  • 0

    5

    10

    15

    20

    25

    30

    35

    40

    0 100 200 300 400 500 600 700

    Correct neutralizer efficiency ppm neutralizer per 1 ppm acid

    correct efficiency factor ppm neutralizer /ppm acid 1984-2017 HT 1955-2017 CaSt

    CaSt theory 20:1 or

    Acid neutralized efficiency per similar volume

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    6

    Catalyst efficiency

    HT actual 35-3.4: 1

    HydrotalciteTheory 10:1

    …A..............................…………………A…….……………A…………..

    …A............A............A....………A………A…………A…………A…………

    ....A…A..…A…A.…A…AA…A….A…A….A…A….…A…A….A…A….A…A.

    Poor Neutralizer

    efficiency

    ppm neutralizer

    per 1 ppm acid

    High

    neutralizer

    efficiency

    ppm

    HCL acid.

  • Acid produced by polyolefin type

    Mitsui neutralizer effective all catalysts and all densities

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    7

    0

    5

    10

    15

    20

    25

    30

    35

    40

    0 100 200 300 400 500 600 700

    PPM of neutralizer per 1 ppm acid

    correct efficiency factor ppm neutralizer /ppm acid incorrect 10:1 effiency factor

    Polyethylene metallic stearates

    Plastomersmetallic oxides Elastomers EPR, EBR, EOR, EPDM

    metallic stearates, metallic hydroxides

    Mitsui new neutralizer range

    Polyproplyene

    Hydrotalcite

    Catalyst efficiency

    mLLDPE

    Decreasing

    density

    ppm HCL

    acid

  • M-Series catalyst neutralizer suggestions:

    October 2018MPI Confidential Developmental ZRxL,P Series

    8

    SUGGESTIONS ppm of acid from TiCl4 Commercial Examples

    Ziegler-NattaCatalyzedPolyolefins g-cat/xxxxg Polyolefin

    ppm Ti in polyolefin

    phenolic AO ppm / phosphite AO ppm Ppm of

    Mitsui M-Series

    HCL = ppm Ti x (141.6/47.9 (ppm/mole)

    1 ppm Ti = 4 ppm HCL1 ppm Mg = 3ppm HCL**

    1gTiCl4 = 25.27% Ti

    1g-cat/50,500g 1kg-cat/50 tons PE

    5 500/1000600

    350.934-0.920LLDPE film grades

    Polyethylene

    1g-cat/25,200g 1kg-cat/25.2 tons PE

    10375/750

    =25% less AO

    800

    70

    0.920-0.910 LLDPE film grades

    1g-cat/12,600g 1kg-cat/12.6 tons PE

    20-25350/700

    =30% less AO 1,000 140-175 0.880-0.909 Plastomers

    Bi-modal HDPE pipe and film grades

    1g-cat/8,400g 1kg-cat/8.4 tons PE

    30350/700

    =30% less AO 1000210

    bi-modal HDPE (Mitsui CX).

    • * ppm XRxL needed to neutralize catalyst acid, stabilized anti-oxidants and protect the polymer from degredation. 20x the HCL concentration.

    • ** HCL from MgCL2 catalyst support which is 2.89 ppm HCL / 1ppm Mg. So, 1ppm Ti + 1 ppm Mg = 7 ppm HCL.

    Increasing

    catalyst

    Efficiency

  • How does Mitsui’s M-Series neutralizer work?

    Proprietary blend designed for:

    4th – 6th generation TiCl4-MgCl2 catalysts.

    polyolefin density ranges 0.640 – 0.965

    Color correction chemistry, Balanced pH and surface area = lowest color.

    Performs excellent with antioxidants per pellet, LAB, YI.

    H/E lubricants reduces shear and heat stress

    Improved polymer stability per FTIR

    Improves antioxidant efficiency per OIT, HPLC

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    9

  • Polyethylene resultsMitsui ZRxL Development in HDPE pipe and LLDPE film resins

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    10

  • Problems with metallic stearates

    and oxides in Polyethylene

    1. Acid scavenging chemistry:

    2. is a corrosive “Lewis acids” (ref.1)

    Lewis acid examples : TiCl4, ZrCl4, ZnCl2, CaCl2, NaCl

    Lewis acids destroy antioxidants and hindered amines (HALS).

    3. has a 114c flash point so carbonizes which

    forms black specs, die smoke and plate out.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    11

  • C

    Problems with metallic stearates

    and oxides at molders

    Black specs

    Molded from 1st extruder pass

    of 0.906g/cc density LLDPE.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    12

    MPI 37L MPI 3L CaSt

  • Polyethylene formulations

    Bi-Modal HDPE 0.03 MI, 0.949 g/cc density

    Extrusion at 90 RPM, Tm 190c *

    Antioxidants: 500 ppm AO 1010 + 500 ppm AO 168

    MPI 7L development vs Controls: CaSt, HT, HT-2

    C6-LLDPE 0.50 MI, 0.917 g/cc density

    Extrusion at 90 RPM, Tm 190c *

    Antioxidants: 500 ppm AO 1010 + 500 ppm AO 168

    MPI 3L development vs Controls: CaSt, ZnSt, ZnO, HT-2

    C6-LLDPE 0.50 MI, 0.917 g/cc density

    Extrusion at 30 RPM , Tm 250c under N2 **

    Antioxidants: 500 ppm AO 1010 +1,000 ppm AO 168

    MPI 737P development vs HT, CaStFeb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    13

    New Fall 2018 developments with 25-30% AO reduction

  • Polyethylene formulations

    C6-LLDPE 0.50 MI, 0.906 g/cc density Extrusion at 30 RPM, Tm 250 c * *

    Antioxidants: 800 ppm AO 76 + 1400 ppm Weston 705T.

    MPI 3L and 37L development vs CaSt

    * Extruder details: 3/4in 20mm SSE with 33:1 L/D with 2 mixing zones Z1 =170 C, Z2 =190 C, Z3 =190 C, Die 190 C, screw RPM =90

    ** Extruder details: 3/4in 20mm SSE with 33:1 L/D with 2 mixing zones Die 250c, screw RPM = 30, Rate 1.5-3.0 kg/hour.

    Molding details: 30 Ton hydraulic injection press (SPEC capable, ASTM, ISO, test bars, 3"x3" GM texture Plaques, machined-in notched Izod bars.) 390/450/450 Deg. F, 2500psi 30 seconds cooling time.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    14

  • HDPE data:

    Bimodal pipe grade 0.947 g/cc

    Blow molding grade 0.950 g/cc

    M-Series 7L development vs calcium stearate and Hydrotalcite

    Extrusion at 90 RPM, Tm 190c

    Antioxidants: 500 ppm AO 1010 + 500 ppm AO 168

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    15

  • M7L protects antioxidants

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    16MPI 7L 32% less HDPE oxidation

    vs HT and 56% less than

    Calcium stearate

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1st Pass 1000ppm CaSt

    5th pass CaSt 1st pass 500ppm HT

    5th pass HT 1st pass 1000ppm MPI 7L

    5th pass MPI 7L 1st pass1010+168

    5th pass 1010 +168

    OIT @200c minutes

  • 420

    469

    324

    222

    437450

    183

    105

    368354

    244

    142

    310 316

    65

    0

    1ST PASS HT-2 MPI 7L CaSt 1010 + 168 5th pass HT MPI 7L CaSt 1010 + 168

    1st vs 5th Extruder Pass 200c.

    IRGANOX 1010 (BY LC) PPM IRGAFOS 168 (BY LC) PPM

    M7L 31% - 80% more AO retained

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    17

    5th pass 7L 80%

    more 168 retained

    vs CaSt

    5th pass 7L 60%

    more 1010 retained

    vs CaSt 1st pass 7L retains 31% more AO vs CaSt

  • M7L reduces extruder pressure in HDPE

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    18

    ZR7L 20% lower

    extrusion pressure

    than HT and ZHT

    0

    20

    40

    60

    80

    100

    120

    Bar Bar Bar Bar bar bar

    Ctrl AO HT HT-2 CaSt MPI 7L

    extruder die pressure in BAR

    1st 3rd 5th

  • 0

    0.5

    1

    1.5

    2

    2.5

    3

    3.5

    Ctrl AO HT HT-2 Cast MPI 7L

    B color

    1 3 5

    M7L lowest color in Bi-modal HDPE pipe grade

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    19

    Melt 190c

  • M7L 40-60% improvement in the quality of HDPE molded parts

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    20

    0

    0.5

    1

    1.5

    2

    2.5

    3

    3.5

    4

    AO only 500 ppm HT-2 1000 ppm CaSt 1000 ppm MPI 7L

    % Standard Deviation from molding 10 HDPE parts

    TS % Std.Dev 1% Flex Mod % Std. Dev

  • M37L and M3L shows no color oxidation in HDPE

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    21

    Melt 287c

    -4

    -2

    0

    2

    4

    6

    8

    0 pass 1st pass 3rd pass 5th pass 0 pass 1st pass 3rd pass 5th pass 0 pass 1st pass 3rd pass 5th pass

    1,000 ppm CalciumStearate

    1,000 ppm MPI 3L 1,000 ppm MPI 37L

    0.950g/cc HDPE pellet YISSE 1.25inch (32mm). 100 RPM at 550F (287c). 0 pass N2

    800 ppm AO 1010 + 800 ppm AO 168 + below catalyst neutralizers

  • C6-LLDPE 0.917g/ccMPI 7L and 37L development

    vs CaSt, ZnSt, ZnO and Hydrotalcite

    Extrusion at 90 RPM, Tm 190c

    Antioxidants: 500 ppm AO 1010 + 500 ppm AO 168

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    22

  • 0.000

    0.500

    1.000

    1.500

    2.000

    2.500

    3.000

    3.500

    4.000

    4.500

    No AO AO HT-2 MPI 7L CaSt ZnSt

    0.917 C6-LLDPE MI 190c/10kg

    0 pass 1 pass 3 pass 5 pass

    M7L stable multi-pass MI

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    23Increasing ppm of stearic acid + Lewis acid cracking the PE.

  • M3L and M7L low color LLDPE

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    24

    -20.00

    -15.00

    -10.00

    -5.00

    0.00

    5.00

    10.00

    15.00

    20.00

    25.00

    MPI 3L1000ppm

    MPI 7L1000ppm

    ZnSt1000ppm

    HT-2500ppm

    CaSt1000ppm

    ZnO 800ppm No AO AO Only500-1010,500-168

    YI from molded tensile bars 1st extruder pass, 3rd and 5th. 70c 6 week oven aging from 3rd pass. Extruder details: 3/4in 20mm SSE 33:1 L/D

    with Z1 =170 C, Z2 =190 C, Z3 =190 C, Die 190 C, screw RPM =90, Screw: mixing head

    YI 1st pass YI 3rd pass YI 5th pass YI 70c 6 wks 3rd pass

    ZnO blue shade pigment color change is very high

  • M3L 30% lower extruder pressure in LLDPE

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    25

    NOTES: ZnO 1st extrusion black die drool and by 5th black powder residue

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

    HT-2 500ppm MPI 7L 1000ppm CaSt 1000ppm MPI 3L 1000ppm ZnSt 1000ppm ZnO 800ppm

    Psi start 1st pass

    PSI finish 1st pass

    Psi start 3rd pass

    PSI finish 3rd pass

    PSI start 5th pass

    PSI finish 5th pass

    Extruder pressure changeZ1 =170 C, Z2 =190 C, Z3 =190 C, Die 190 C, screw RPM =90, Screw: mixing head

    MPI 3L 30% less

    pressure than ZnO,

    25% less than ZnSt

    20% less than CaSt

  • M3L and M7L 60-75% improvement in quality in LLDPE

    Feb 24-27, 2019

    Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    26

    Polymer Performance Quality

    Quotient = Higher number

    better quality

    HDPE 1% mod / Std. Dev

    LLDPE TS / Std. Dev

    Red Part to part Std.

    Dev. Lower number

    better quality

    0

    20

    40

    60

    80

    100

    120

    AO only HT-2 CaSt M7L CaSt ZnSt HT-2 M3L M7L

    HDPE LLDPE

    HD 1% Mod, LL TS /StdDev StdDev

  • C6-LLDPE 0.917g/cc

    New M-Series M737LP developments NOV 2018

    vs calcium stearate and Hydrotalcite1, 3, 5 Extrusion at 30 RPM, Tm 250c under N2

    Antioxidants: 500 ppm AO 1010 +1,000 ppm AO 168

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    27

  • M737P no yellow 1-5 extruder passes

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    28

    -6

    -5

    -4

    -3

    -2

    -1

    0

    1

    2

    3

    CaSt 1000 ppm HT-1 500 ppm M737LP 800 ppm M737LP 1000 ppm M737LP 800 ppm, 25%less AO

    M737LP 1000 ppm,30% less AO

    Pellet YI yellowness Index. AO only YI = 5.6

    1st pass 3rd pass 5th pass

  • M737P even with 30% less AO more stable than

    the Calcium Stearate Control

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    29

    0

    0.1

    0.2

    0.3

    0.4

    0.5

    0.6

    0.7

    0.8

    0.9

    1

    CaSt 1000 ppm HT-1 500 ppm M737LP 800 ppm M737LP 1000 ppm M737LP 800 ppm, 25% lessAO

    M737LP 1000 ppm, 30%less AO

    MFR 230c, 2.16kg AO only 8.33g/10min.

    1st pass 3rd pass 5th pass

  • M737P high oxidative stability even with 30% less antioxidants

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    30

    0

    50

    100

    150

    200

    250

    300

    AO only CaSt 1000 ppm HT-1 500 ppm M737LP 800

    ppm

    M737LP 1000

    ppm

    M737LP 800

    ppm, 25% less

    AO

    M737LP 1000

    ppm, 30% less

    AO

    OIT (oxygen induction time) 200c in minutes

    1st pass 3rd pass 5th pass

    M737LP 45-145% increase in oxidative stability

  • C6-LLDPE 0.906 g/ccMitsui’s M-Series M3L and M37L compared to Calcium Stearate

    Extrusion at 30 RPM, Tm 250 c

    Antioxidants: 800 ppm AO 76 + 1400 ppm Weston 705T.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    31

  • M3L and M37L show improved MI stability

    in LLDPE plastomer

    Feb 24-27, 2019

    Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    32

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1200 ppm CaStcontrol

    1000 ppm Mitsui 3L 1000 ppm Mitsui37L

    LLDPE 0.906g/cc MFR 230c/10kg vs 1,3,5 extrusions 246c

    1,3,5 % change 1st pass 3rd pass 5th pass

  • Mitsui 3L and 37L show excellent low YI color

    in LLDPE plastomer

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    33

    -15

    -10

    -5

    0

    5

    10

    15

    1200 ppm CaStcontrol

    1000 ppmMitsui 3L

    1000 ppmMitsui 37L

    LLDPE 0.906 YI E313; 1, 3, 5 extrusion passes 246c

    1st pass 3rd pass 5th pass

  • FTIR oxidation values vs YI raw data

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    34

    y = 7.7803x - 7.11R² = 0.9267

    -12

    -10

    -8

    -6

    -4

    -2

    0

    2

    4

    6

    8

    10

    0 0.5 1 1.5 2 2.5

    Carbonyl Index (area) vs. YI

    FTIR raw data M3L 1st M3L 5th M37L1st M37L5th CaSt 1st CaSt 5th

    Corr Area

    1/cm

    CH2 group 720 2.319 2.865 4.223 1.28 3.71 3.627

    CH2 group 730 1.246 1.085 1.124 1.953 1.354 0.139

    C-C bond 1465 0.842 0.481 1.781 0.946 1.301

    C=O 1720 0.062 0.137 0.277

    C=O 1740 0 0.039 0.193 0.549 0.356 0.369

    OH 3603 1.528 2.013 1.306 3.468 1.883 1.505

    Ratio C=C/C2 1740/730 0 0.035945 0.171708 0.281106 0.262925 2.654676

    Ratio C=O/C2 1720/730 0 0 0 0.031746 0.101182 1.992806

    Pellet YI -8.97 -5.35 -9.34 -4.78 -6.12 8.33

  • M Series no PE oxidation and lowest color.

    CaSt high oxidation even with low color.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    35

    -12

    -10

    -8

    -6

    -4

    -2

    0

    2

    4

    6

    8

    10

    CaSt 1st pass CaSt 5th pass M3L 1st pass M3L 5th pass M37L 1st pass M37L 5th pass

    FTIR PE oxidation vs YI pellet color

    Carbonyl 1720/730 + 1730/730 YI

  • M-Series recycle improvements + odor reduction

    Performance:

    1. 45-145 % increased time to oxidize. (DSC OIT oxygen induction time at 200c.)

    2. Antioxidant is preserved per LC analysis:

    30% increase 1st extruder pass

    60-80% increase 5th extruder pass

    3. Average 50-90% less degredation - per FTIR. (C=O carbonyl @1720-1740-cm / C2 % @ 730-cm)

    Value: average 50-90% increase in recyclability and odor reduction due to antioxidant preservation and reduced polymer oxidation.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    36

  • Mitsui Plastics Inc. M-Series for Polyethylene Summary

    Market:

    Effective in all 4th – 6th generation ZN catalysts.

    Replace 800 -1,000 ppm metallic stearate or metallic oxide with equal ppm of M-Series.

    Improved Quality:

    45-145 % increased time to oxidize. (OIT DSC oxygen induction time at 200c.)

    30% increase in antioxidant retention - per HPLC 1st extruder pass. 60-80% by 5th pass.

    40-50% reduction in film gels – per customer

    Average 50-90% less degredation - per FTIR. (C=O carbonyl @1720-1740-cm / C2 % 730-cm)

    Improved: Performance:

    20-30% reduction in extruder pressure. Possible, lower melt fracture.

    40-60% increase in LLDPE tensile strength and HDPE Flex. Mod.

    40-75 % reduction in part to part Std. Dev.

    Savings + improved quality and performance – up to $500,000 / each 1B lbs.

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    37

  • M-Series powder and pellet forms

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    38

    Made in Germany (pellets in mm)

    Made in USA

  • For further information and samples:

    Reference:

    Please contact:

    Don Beuke – Mitsui Plastics Inc.

    918-914-2947

    [email protected]

    REF 1. Mechanism of Lewis Acid Metallic stearates and oxides

    ZnCl2 CaCl2 are Lewis acids because it can accept an electron pair from a

    Lewis base like OH- Tert-butyl phenolic antioxidant.

    A Lewis acid is a molecule that can accept an electron pair and a Lewis base is

    a molecule that can donate and electron pair. When a Lewis base combines

    with a Lewis acid an adduct is formed with a coordinate covalent bond.

    i.e. CaCl₂ + 2 (OH- T-butyl phenol) —->Ca(OH)₂ + 2Cl +2 H2O 4HCL + O2

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    39

    mailto:[email protected]

  • Thank you SPE Polyolefins Conference – Dr. Thoi Ho Additives Chair.

    Our polyolefin customers – you know who you are!

    Mitsui Plastics Inc. USA – financial support (many RINGI’s)

    Amazing plastics laboratories: Nobukatsu Shigi – Japan, Dr. Amit Dharia – USA,

    Feb 24-27, 2019Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    40

  • The values and information represented herein are typical and should not be considered to represent any specification. Mitsui Plastics, Inc. ("Mitsui")does not guarantee the reproducibility of the data represented herein in customer's own or contracted testing facility. Mitsui makes no warranty, express or implied, regarding merchantability or fitness for a particular purpose. Freedom from the infringement of a patent of Mitsui or any other party is not to be inferred. Customer is solely responsible to verify the suitability of the material for their intended use. In no case shall Mitsui have any liability to any person in respect of any loss, claim, damages, costs or liability arising from reliance on any information contained in this report or use of this report.

    Feb 24-27, 2019

    Mitsui Plastics Inc. - Disclaimer

    Mitsui Plastics Inc. presentation to SPE Polyolefins Conference

    41