Alfa Laval Innovations
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2 Alfa Laval Innovations Carlsberg Technology Seminar, 10 April 2018 Alfa Laval Brewery Systems Søborg, Denmark
3 Agenda Main topics: High yeild dry hopping based on Alfa Laval Iso-MIX Next generation high speed separators with emotion and Integral disc Additional solutions to discuss during meetings with teams: Alfa laval LKH Prime Alfa Laval TJ40G Rotary Jet Head Alfa Laval Foodec decanter Mixed-fuel boilers using stripped ethanol Alfa Laval Slide 3
4 Dry Hopping with IMXD Alyce Hartvigsen
5 Problem: Efficient Dry Hopping Alfa Laval Slide 5
6 Problem: Dry Hopping Process Issues Slugs of hop solids Blockages of lines, HEX, filters Carry-over of solids Product losses Unplanned down-time/outages Increased waste streams Alfa Laval
7 Solution: Dynamic Dry Hopping More effective dispersion of hops into beer Faster and more efficient aroma/flavour extraction Shorter hop residence times in beer Homogenization of hop particles during transfer Efficient separation of hops from beer Reduction of beer losses Reduction of process times Alfa Laval Slide 7
8 Iso-Mix External Drive (IMXD) Motor-driven Rotary Jet Mixer Tolerates high particulate loads Flexible hops introduction method Fast dispersion and flavour extraction Homogenization of feed to centrifuge Reduced hop residence time Reduced beer losses More efficient aroma/flavour extraction Alfa Laval Slide 8
9 IMXD system with hop slurry injection Prepared hop slurry dosed into IMXD loop during circulation Alfa Laval Slide 9
10 10 Efficient hop removal & reduced losses Homogeneous solids loading to centrifuge inlet Complete removal of hops solids and regular discharge intervals Reduced losses means less waste streams SAMPLE OF SOLIDS DISCHARGE PRE POST CENTRIFUGE
11 Customer results with IMXD Alfa Laval Slide 11
12 Summary: Dry hopping with IMXD Significant reduction in process time & energy consumption Significant reduction in beer losses & waste streams Complete hop removal by centrifugation Faster and more efficient aroma/flavour extraction No significant differences in beer flavour Potential for larger product batches Potential for higher dry hop dosing Additional benefits with mixed fermentation and accelerated cooling (reduced energy consumption) Product ROI << 1 year Alfa Laval Slide 12
13
14 Creating values by innovation Latest innovations in centrifugation Fernando Jimenez Global Sales Brewery BU High Speed Separators Tumba Sweden
15 Focus on R&D Launching new products every year, whereof 8-12 separators More than patents, whereof appr. 500 separator related Investment (2016): MEUR 87 = 2.3% of total net sales. For separators 4,8% of net sales
16 Alfa Laval design Philosophy Power Consumption Center-tocenter Bactofuge Solid handling Separation performance Cost
17 Innovations in centrifugation emotion Top Stream Unidisc Center to Center
18 Center to Center Fundamentals of the fully hermetic bowl
19 Center to Center design (C2C) Gentlest feed acceleration V g = d2 ρ 18μ ω²r d 2 Vg 4
20 , 4rpm,185 kg
21 Flow Power Paring disc Centripetal Pump (Static) r u ² radius of level ring ω² Bowl Speed Q Flow P Q = ρqω²r u ²
22 Center to Center Summary Smooth acceleration of the feed minimizes yeast micronization (particlle splitting) increasing exponentially sedimentation velocity. No product Oxidation, No aroma / hop oil stripping and virtually No Oxigen Pick up. Significant reduction in power consumption. Up to 70% reduction compared to traditional top feed bowl design. Bowl design capable to operate in a wide range of flows without any further adjustment.
23 edrive (patented innovation) Mechanical simplicity: rotor is an integral part of the bowl spindle. Fewer parts: No motor bearings, motor shaft or flat belts. Less moving parts, less energy loss, less heat generation, less need for cooling. Extended service intervals.
24 emotion running Lean & Cool Low pressure technology for high speed centrifuges
25 Separator Power Consumption Contributions to HSS power consumption PQ: Flow Power Pf : Friction from paring disc Pair: Air Friction (bowl-casing) Pair; 20% Pother; 10% Pq; 50% Pother: Bearings, transmission, seals, discharge system etc. Pf; 20% Power = PQ + Pf + Pair + Pother Idle Power
26 emotion Running Lean & Cool - Theory Air friction power (bowl-casing) theory F air 3 5 P c R BREW 701 centrifuge bowl periphery speed: 708 km/h
27 emotion Running Lean & Cool - Technology Low air pressure in centrifuge casing using vacuum pump 0,1 bar 90 % vacuum 0,5 bar 50 % vacuum 0,3 bar 70 % vacuum Mont Blanc Mount Everest emotion centrifuge
28 0,1 bar ~ m
29 emotion Running Lean & Cool Intermittant evacuation of air outside the bowl with liquid ring pump Reduces idling power Better hygiene (less burning-on) improved internal aerodynamics with reduced secondary flow vortices Cooler surfaces on the outside of the separator Reduced sound level of separator Reduced cooling water consumption Facilitates PX solids discharge
30 emotion Running Lean & Cool Power consumption to system Open inlet & paring disc 1,2 kwh/m % Semi Hermetic 0,7 kwh/m3 kw % - 40% BREW 2001 with paring disc BREW 2001 hermetic BREW 2000 Full Hermetic 0,45 kwh/m3 emotion 0,28 kwh/m m3/h
31 emotion Running Lean & Cool emotion OFF emotion ON
32 emotion Running Lean & Cool
33 UniDiscs Boosting Separation Performance to new boundaries
34 UniDiscs Theory Lambda Flow pattern between rotating discs. Radial-tangential velocities Substancial efficiency optimisation possible by reducing lambda factor. h sin
35 UniDiscs Technology Radical production technology innovation. No welding. Micro-caulks as distance/spacers between discs Discs are thinner and caulk height lower. Disc stack can hold more discs increasing efficiency.
36 UniDiscs Benefits Equidistant space between discs. Separation area is used more efficienctly. Optimal disc stack flow pattern. Significant improvement of Flow between discs. No maldistribution (unequal resistances from flow) which greately improves separation efficiency. Better cleanability. Formed from one single element. Less risk of contamination. 30% Flowrate increase with equivalent separation performance.
37 Top Stream Improved yeast handling in disc stack centrifuges for breweries using continuous solids discharge design
38 Traditional Mechanical separation liquid/solids 5000 g Liquid Solids 0,5 mm Flow between the discs
39 Top Stream Process Continuous solids stream Clarified beer stream Conventional solids discharge stream Feed stream
40 Top Stream process flows Continuous Solids stream Clarified beer stream Intermittent solids discharge stream Feed stream
41 Top Stream: Continous Yeast flow in pipes over top disc Yeast concentrate flow velocity v G = d2 ( ρ p ρ l ) rω 2 18 μ Particle settling velocity ~ flow rate ~ (rotation speed) 2
42 Top Stream Technology Hermetic Separator with continous concentrate flow sectors over top disc Fully hermetic design. No Oxygen pick up Hybrid separator. It can operate in continious discharge mode or intermittent discharge. Higher solids handling capacity than conventional self cleaning separators. Increase of beer yields. Beer recovery out of tank bottoms in continous mode. Minimum temperature pick up. No need of beer recirculation. Absence of low flow transitions. Centrifuge solids space is no longer a process constraint.
43 Top Stream Summary Not limited by solids content at the inlet. Bowl solids space is not longer a limitation to reach high flows with superior clarification performance High flexibility in feed concentrations of solids Full control characteristics of effluent and/or yeast concentration Low power consumption Yeast Outlet. It is not contaminated with operating/flushing water High yeast viability ( > 95% vital yeast viability) Air/foam free design allows a continuous measurement of solids concentration from outlet, for process control
44 Innovation in centrifugation Summary emotion 30 60% decrease in power consumption v.s traditional brewery separator Less CIP need Reduces cooling water consumption Top Stream Increased solids handling capacity High yeast viability Lower power consumption Center to Center Integral discs 30% higher capacity in existing machines Less CIP need 30 60% decrease in powe consumption v.s traditional brewery separator Optimal beer handling Low product losses No oxygen pick-up
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