The Art of Mixing, Anaerobic Digesters
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1 The Art of Mixing, Anaerobic Digesters Dr Hara Papachristou Process Engineer 25th October 2011 BHR Group 2011 BHR Group is a trading name of VirtualPiE Limited
2 Aims Highlight the importance of getting digester mixing right Provide an overview of the current state of the art in digester mixing BHR Group
3 Contents Importance of digester mixing Mixing objectives and design criteria Measuring and modelling mixing performance Digester mixing state of the art Digester and Sludge Mixing Software BHR Group
4 Background Increasing number of digesters, mixing and holding tanks are in use Wide range of mixer types/sizes Few mixing criteria established or applied Reliance on mixer suppliers, no independent design information No link between rheology and mixer sizing Variable success of installed mixers BHR Group
5 Industry Needs Why is mixing so increasingly important? Thicker feed sludges to improve throughput, leading to thicker digestate Smooth out variability in feed physical properties Maximise gas production Maintain uniform digester temperature Avoid built-up deposits on digester floor Dilute inhibitory substances entering digester Avoid short circuiting to maximise pathogen kill BHR Group
6 Mixing Objectives What should the mixer achieve? Blending feed sludge into the bulk Generate the desired flow pattern Minimise dead or stagnant zones Avoid solids accumulation Scum drawdown Enable tank emptying BHR Group
7 Defining Mixing Criteria Feed Slurry Blending Blend Time: time taken to achieve a predetermined degree of concentration homogeneity 90% blend time: the time taken for concentration fluctuation to be within +/- 10% of the mean concentration Typically, 90% or 95% blend times of 1 to 2 hours are specified for digesters Active volume The non stagnant volume Typically, 90% or 95% specified Extend of short circuiting BHR Group
8 Modelling Performance Published Design Information Digester mixer design Chemical process mixer design Physical Modelling Clear simulants for slurry & feed Velocity and blend time measurements Wash out curves Computational Fluid Dynamics Flow patterns, velocities and blending BHR Group
9 Digester Mixer Design Consideration Digester shape (base & aspect ratio) Feed & digestate rheology Location of inlets & outlets Digester feed rate & cycle Digester flow pattern & residence time Mixer type and size BHR Group
10 State of the Art Feed location BHR Group
11 State of the Art Impellers BHR Group
12 State of the Art Jets BHR Group
13 State of the Art (a) Sparger A Unconfined Gas Continuous or sequential gas addition through the nozzles No difference for low viscosity digestate Sequential superior for high viscosity digestate x x Inlet position (b) Sparger B x Inlet position x 3 2 BHR Group
14 WWM Scope for Digester Mixing CR8239 Sludge Tank & Digester Mixing Research Report CR8237 Digester & Sludge Tank Mixing Design Guide Mixer design, rating, and selection guide Linked to performance criteria Sludge rheology dependent Based on physical modelling and CFD BHR Group
15 Digester & Sludge Tank Mixing Software Aims: Enable easier and practical application of the paper design guidelines Allow range of mixing scenarios based on combinations of different tank geometries, sludge properties, mixer type Allow rating of digester mixing performance BHR Group
16 Digester & Sludge Tank Mixer Software Excel based software Non newtonian fluids (Power Law and Herschel Bulkley) Transitional and turbulent regimes Jet and submersible mixers Impeller mixers (focus on axial impellers) Unconfined gas mixers Two primary criteria Blend time Active or cavern volume calculations BHR Group
17 Digester & Sludge Tank Mixer Software BHR Group
18 Digester & Sludge Tank Mixer Software BHR Group
19 Digester & Sludge Tank Mixer Software BHR Group
20 Thank you Hara Papachristou Water, Environment & Power (WEP) Fluid Systems Academy Process Enquiries: BHR Group 2011 BHR Group is a trading name of VirtualPiE Limited
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