Transcript Slide 1

STORMS - Key Processing Points For Dow PU Systems
Andrew Davies
Introduction
 The aim of this presentation is to help achieve better success at trials and hence faster
customer approval. We will highlight the importance of correct material handling and
conditioning.
 Mercury is a very forgiving and versatile catalyst in terms of:
• Delayed action cure profile with fast demould capability.
• Versatile amongst DIPRANE™ and HYPERLAST™ product groups (spray, cold-cure)
• More forgiving than other catalyst groups in variety of environments
• More forgiving to a variety of ‘handling’ methods
 The Dow mercury alternatives address the majority of the above characteristics
however the non mercury alternatives
• require better, more efficient mixing of polyol components
• require better control of temperatures for both components and moulds.
• tend to be more moisture sensitive
Hence the importance for following the principals of STORMS
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WHAT IS STORMS?
STORMS - The Definition
Stir Polyol
Temperature Control
Operator Engagement
Ratio Control
Moisture Tolerance
Stir Components Together
Stir Polyol
 Non-mercury catalysed products require better mixing than mercury catalysed
products because:
 lower catalyst levels need better dispersion to gain different effects
 desiccants need to be thoroughly mixed to enhance moisture control
 homogeneous mixing is needed to realise full range of properties
 this will help ensure the additives package within polyol is full effective
 Drums and kegs must be handled as follows;
 Melted and conditioned to correct temperatures as indicated on the Technical
Data Sheet (TDS)
 Rolled/tumbled or mixed with collapsible/helicoidal stirrer for minimum 30
mins. ensuring minimum air entrapment (see next slide)
 The machine tank handling the polyol will require degassing and then constant
agitation by either or both:
 recirculation at rate so as not to introduce air
 keeping the agitator on, again so not to introduce air
Types of Drum Mixing
Drum Roller
Drum Tumbler
Bung Mixer/transfer pump
Drum Attach Mixer
Temperature Check
 Proper temperature control is more critical for non-mercury based systems due
the use of more temperature sensitive catalysts
 Polyol, prepolymer and mould temperatures must be adhered to – generally the nonmercury catalysed systems require increase in either or both the liquid temperatures
or mould temperatures
 Check and familiarise yourselves with the most up to date technical datasheet
 Systems processed at temperatures lower than datasheet recommendation can
lead to some of the following effects:
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Longer pot-life
Slower demould
In-complete cure
Sticky surface effects – most critical for open casting that requires flaming
Reduced physical properties
Duller surface finish
Shrinkage effects
Temperature Contd.
 Systems processed at temperatures higher than datasheet recommendations can result
in:
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Faster gel times so restricting casting size
Inability to fill the mould
Air entrapment/bubbles
Difficulties when hand casting
System
HYPERLAST™
200
HYPERLAST™
201
HYPERLAST™
100
HYPERLAST™
101
DIPRANE™ 53
DIPRANE™ 530
Polyol
Temperature*
20-30
20-30
35-40
35-40
35-40
50 – 55
Prepolymer
Temperature*
20-30
20-30
25-40
25-40
35-40
50 – 55
Mould
Temperature*
70 - 80
80 - 90
70-90
80 - 95
70 - 90
80-100
Demould
Time
* Temperature °C
15-20
15-25
20 - 30
20 - 30
30 - 40
15 - 40
Typical properties – not to be construed as specifications
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Pot-life Comparisons Mercury Catalysed Grades
vs. DIPRANE™ C530/85
200000
180000
160000
Viscosity (Poise)
140000
120000
DIPRANE™ 53/85
100000
DIPRANE™ 530/85
DIPRANE™ 54/85
80000
60000
40000
20000
0
0
1
2
3
4
5
time (mins)
6
7
®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow
8
9
10
Three Component Requirement for Catalysed
Extender
140.0
E
x
o 120.0
t
h
e 100.0
r
m
-------- DIPRANE™ 53/85 CX
80.0
T
e
m 60.0
p
e
r 40.0
a
t
u 20.0
r
e
-------- DIPRANE™ 530/65A + CA
Some users currently taking Three Component DIPRANE™
with CX may need to use the DIPRANE CA in order to
ensure efficient demould at higher hardness.
0.0
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56
Time at 10 second intervals (+100)
®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow
Operator Engagement
 New products will have some differences. It is imperative that the Operators and
production personnel are made fully aware of the requirements and understand the
differences between the traditional mercury containing and the new non-mercury
systems
 Attention should be given to the product documentation and drum labelling
 Material Safety Data Sheet (MSDS) should be available and read by production
operators and supervisors
 Data sheet information on material conditioning, handling should be understood
 Data sheet information on temperature for materials and moulds must be adhered to
 Data sheet information for ratio of components must be adhered to
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Ratio Check
 The ratio must be worked out to ensure the correct proportion of –OH groups versus –NCO
groups to achieve full cure and property realisation.
 The materials should be mixed together to a ratio tolerance no greater than 1% by weight
 Engineering Elastomer datasheets quote ratios as ‘parts’ polyol to 1 part prepolymer.
 DO NOT ASSUME THE MIX RATIOS ARE THE SAME AS BEFORE.
 The development of the mercury alternatives has led in some circumstances to a slight
difference in mix ratio versus its predecessor, for example
 DIPRANE™ 530/85 is 0.92: 1 by weight versus 1:1 for the mercury catalysed grade
 ALWAYS CONSULT THE TECHNICAL DATASHEET – NEVER ASSUME.
 Ensure your customer has the correct and current Technical Datasheet
 Polyol rich castings can lead to soft product with reduction in physical properties and poor
output.
 Isocyanate rich castings can lead the product to be more susceptible to moisture effects, slow
demould, increased post hardening and poor physicals.
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Moisture
 Non-mercury catalysed systems are usually more susceptible to moisture leading to
bubbles or foaming in the casting and so care needs to be taken as follows:
 Polyols must be kept sealed until required
 Replace lids on part filled drums – especially in regions where atmospheric humidity is high
 The elevated temperatures that non-mercury catalysed systems require are more susceptible to moisture
ingress
 Containers for mixing must be clean and dry before use when mixing plugs or decanting
samples.
 Samples sent back to Dow at Birch Vale, UK for analysis must also be clean, dry, sealed
and fully filled – It is mandatory that these are labelled correctly and accompanied by
MSDS
 Polyols contain a moisture scavenger – this must be totally mixed prior to decanting to
keep it efficient
 Machine polyol (and prepolymer) tanks MUST have a dry air supply and also be sealed.
Moisture Contamination
Isocyanate
Group
(R” NCO)
Unstable
intermediate
product
Substitute Urea
R” HN - C(O) - NH – R
Water
(H - O - H)
Carbon
Dioxide
(O - C - O
Stir components together
The polyol and isocyanate must be thoroughly mixed together to achieve a homogeneous
material at the correct ratio to realise full physical properties.
Stir the material either:
 By hand – depending on pot-life and size of casting using following guidelines:
 Condition as per datasheet temperatures
 Weigh out appropriate amounts of polyol and prepolymer
 Mix between 30 seconds to 1 minute depending on casting size with stirrer/spatula
 Transfer mix to another container
 Vacuum degas to remove air (minus 1 bar for 30 sec to 1 minute depending on gel
time)
 Pour into suitable mould at preconditioned temperature as indicated on TDS.
 By machine
 Conditioned and vacuumed in accordance to TDS and machine specification.
To enable fast and efficient success at trials always
remember:
STORMS