de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
de - Beste verfügbare Techniken (BVT) - Umweltbundesamt de - Beste verfügbare Techniken (BVT) - Umweltbundesamt
Chapter 6 Economics Prevention of problems will be more cost effective than later plant retrofits, loss of production or end-of-pipe treatment of waste. Driving force for implementation Improved economics, increased production, improved product quality. References to literature and example plants [104, BHR Group, 2005] 396 Dezember 2005 OFC_BREF
6.2 Process intensification Description Chapter 6 Most OFCs are manufactured in batch stirred vessels, which are used for blending, reaction and separation (eg crystallisation, liquid-liquid extraction). Such technology has the benefit of being well understood and highly flexible. However, as described in Section 6.1, performance is often suboptimal. Even when mixing in stirred vessels is optimised, fundamental limitations on their performance (e.g. rate of mixing and heat transfer) can still mean loss of performance on scale up (see Section 6.1). Moving from batch to small scale, continuous, intensified reactor technologies has the potential to make step changes in environmental performance. A wide range of such Process Intensification (PI) technologies is available for single and multiphase processes, including: • static mixer reactors • ejectors • combined chemical reactor-heat-exchangers (HEX reactors) • spinning disk reactors • oscillatory flow reactors • ‘higee’ technology. PI technologies are complementary to microreactor technologies (Section 4.1.4.6), and can be applied where larger production rates are required (10 – 10000 tonnes per year) and the ‘numbering up’ philosophy for microreactors becomes impractical. Achieved environmental benefits These will vary from application to application, but typical examples of environmental benefits from the application of PI are: • 99 % reduction in impurity levels in a hydrosilylation process resulting in a more valuable product whilst reducing excess reagents by around 20 % and removing requirements for an additional solvent • >70 % reduction in energy usage (typical figure for a range of processes studied – achieved through substantial reduction in the time spent mixing and the ability to integrate heat) • >99 % reduction in reactor volume for potentially hazardous processes, leading to inherently safe operations. Maximum environmental benefits can be achieved through combination of PI with green chemistry (Section 4.1.1), solvent selection (Section 4.1.3), and alternative synthesis and reaction conditions (Section 4.1.4). Cross-media effects Wahrscheinlich keine. Operational data Some additional development time may be needed for an intensified, continuous process, and care is needed with start up and shut down procedures. Once operating under steady state conditions, such technologies will provide reliable processes, with minimal manual interventions required and batch to batch variability avoided. OFC_BREF Dezember 2005 397
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- Seite 421 und 422: 5.2.4.3 Entfernung von Lösemitteln
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- Seite 450 und 451: Glossar EC 50 Acute toxicity level
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- Seite 454 und 455: Glossar VSS Volatile Suspended Soli
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6.2 Process intensification<br />
Description<br />
Chapter 6<br />
Most OFCs are manufactured in batch stirred vessels, which are used for blending, reaction and<br />
separation (eg crystallisation, liquid-liquid extraction). Such technology has the benefit of being<br />
well un<strong>de</strong>rstood and highly flexible. However, as <strong>de</strong>scribed in Section 6.1, performance is often<br />
suboptimal. Even when mixing in stirred vessels is optimised, fundamental limitations on their<br />
performance (e.g. rate of mixing and heat transfer) can still mean loss of performance on scale<br />
up (see Section 6.1).<br />
Moving from batch to small scale, continuous, intensified reactor technologies has the potential<br />
to make step changes in environmental performance. A wi<strong>de</strong> range of such Process<br />
Intensification (PI) technologies is available for single and multiphase processes, including:<br />
• static mixer reactors<br />
• ejectors<br />
• combined chemical reactor-heat-exchangers (HEX reactors)<br />
• spinning disk reactors<br />
• oscillatory flow reactors<br />
• ‘higee’ technology.<br />
PI technologies are complementary to microreactor technologies (Section 4.1.4.6), and can be<br />
applied where larger production rates are required (10 – 10000 tonnes per year) and the<br />
‘numbering up’ philosophy for microreactors becomes impractical.<br />
Achieved environmental benefits<br />
These will vary from application to application, but typical examples of environmental benefits<br />
from the application of PI are:<br />
• 99 % reduction in impurity levels in a hydrosilylation process resulting in a more valuable<br />
product whilst reducing excess reagents by around 20 % and removing requirements for an<br />
additional solvent<br />
• >70 % reduction in energy usage (typical figure for a range of processes studied – achieved<br />
through substantial reduction in the time spent mixing and the ability to integrate heat)<br />
• >99 % reduction in reactor volume for potentially hazardous processes, leading to<br />
inherently safe operations.<br />
Maximum environmental benefits can be achieved through combination of PI with green<br />
chemistry (Section 4.1.1), solvent selection (Section 4.1.3), and alternative synthesis and<br />
reaction conditions (Section 4.1.4).<br />
Cross-media effects<br />
Wahrscheinlich keine.<br />
Operational data<br />
Some additional <strong>de</strong>velopment time may be nee<strong>de</strong>d for an intensified, continuous process, and<br />
care is nee<strong>de</strong>d with start up and shut down procedures. Once operating un<strong>de</strong>r steady state<br />
conditions, such technologies will provi<strong>de</strong> reliable processes, with minimal manual<br />
interventions required and batch to batch variability avoi<strong>de</strong>d.<br />
OFC_BREF Dezember 2005 397