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STORMS - Key Processing Points For Dow PU Systems

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.

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STORMS - Key Processing Points For Dow PU Systems

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  1. STORMS - Key Processing Points For Dow PU Systems Andrew Davies

  2. 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 ®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow

  3. WHAT IS STORMS?

  4. STORMS - The Definition Stir Polyol Temperature Control Operator Engagement Ratio Control Moisture Tolerance Stir Components Together

  5. 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

  6. Types of Drum Mixing Drum Attach Mixer Drum Roller Drum Tumbler Bung Mixer/transfer pump

  7. 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 non- mercury 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: • 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

  8. Temperature Contd. • Systems processed at temperatures higher than datasheet recommendations can result in: • Faster gel times so restricting casting size • Inability to fill the mould • Air entrapment/bubbles • Difficulties when hand casting Typical properties – not to be construed as specifications ®TM Trademark of The Dow Chemical Crompany (“Dow”) or an affiliated company of Dow

  9. Pot-life Comparisons Mercury Catalysed Grades vs. DIPRANE™ C530/85 ®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow

  10. Three Component Requirement for Catalysed Extender ®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow

  11. 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 ®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow

  12. 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. ®TM Trademark of The Dow Chemical Company (“Dow”) or an affiliated company of Dow

  13. 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.

  14. 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

  15. 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.

  16. To enable fast and efficient success at trials always remember: STORMS

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