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PHOENICS User Group Meeting

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Title: PHOENICS User Group Meeting


1
PHOENICS User Group Meeting
  • Benelux User Group
  • Aristo Centre
  • Eindhoven
  • Netherlands

May 2005
2
Modelling Discharges from Rooftop Stacks in
Confined Environments
  • A CFD presentation
  • by
  • Dr. Paddy Phelps
  • ( Flowsolve Ltd )

3
Eindhoven 2005Outline of Presentation
  • Presentation encompasses the results of three
    different projects, performed over a period of
    time
  • Each project used CFD to satisfy a different
    objective

4
PROJECT 1
  • A Classical Planning Consent Project
  • Using simulations to determine the dispersion
    consequences of releases from a yet to be
    constructed facility
  • Predictions assist building services design team
    to arrive at an effective venting strategy

5
PROJECT 2
  • A Diagnose and Remedy Project
  • CFD simulations used to investigate cause of
    environmental nuisance or potential hazard, and
    assist in design of appropriate retro-fit
    remedial measures

6
PROJECT 3
  • A Compare and Contrast Project
  • Comparing possible extract strategies, for a
    situation where tall stacks cannot be used for
    aesthetic / planning reasons

7
PROJECT 1
  • PREDICTING THE
  • DISPERSION CONSEQUENCES
  • OF FUME RELEASES
  • FROM BUILDING ROOF-TOP STACKS

8
Consequences of release dispersion from an
urban university research facility
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Sample Results Obtained
  • Conclusions

9
Emissions Dispersion Study Industrial Context
  • A research facility is housed in a pre-existing
    building on the campus of a city-based UK
    University.
  • The site is a built-up area with a mix of private
    and college accommodation, shops, and university
    laboratories and buildings in the immediate
    vicinity.

10
Emissions Dispersion Study Industrial Context
  • It is planned to construct a large extension to
    the existing research building, effectively
    doubling its size

11
Flow Geometry Close-up
12
Emissions Dispersion Study Industrial Context
  • The building extension will contain new research
    laboratories, from which air and fume-cupboard
    extracts will need to be vented thoughtfully and
    considerately to atmosphere .

13
Emissions Dispersion Study Industrial Context
  • Low levels of allergens may remain in the vented
    fumes
  • Whilst not always necessarily toxic, the releases
    may be tainted by unpleasant aromas
  • There is a history of local complaints about poor
    dispersion of unpleasant smells

14
Emissions Dispersion Study Industrial Context
  • The building extension will create a significant
    additional impediment to the local ambient
    airflow
  • This may have a big influence on the air flow
    patterns at the vent stack release points

15
Emissions Dispersion Study Industrial Context
  • Will releases from the roof-top stacks of the
    research building have adequate dilution /
    dispersion consequences ?
  • Could effluent plumes impinge upon openable
    windows or HVAC intakes in nearby buildings, or
    public access areas ?
  • If a hazard to the public exists, what is the
    extent, and how may it be eradicated ?

16
Flow Geometry Close-up
17
Consequences of release dispersion from an
urban university research facility
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Sample Results Obtained
  • Conclusions

18
Emissions Dispersion Study Methodology
  • Use simulation tools to predict trajectory of
    effluent discharge
  • Determine dispersion envelope of potentially
    toxic components in effluent
  • Confirm any new discharges will not exacerbate
    existing discharges

19
Emissions Dispersion Study Objectives
  • Model predictions will provide input to the
    design of discharge arrangements which will lead
    to acceptable environmental impact

20
Emissions Dispersion Study Objectives
  • What constitutes acceptable environmental
    impact ?
  • The Plume Core is diluted and dispersed to a safe
    level at nearby
  • HVAC intakes
  • Opening windows
  • Public access areas

21
Criterion of Acceptability
  • A safe level is taken in this instance to be a
    dilution level of 1104 ( i.e. a concentration of
    100 ppm ) from stack release
  • The plume core is the spatial envelope of this
    critical dilution / concentration

22
Overview of Release Conditions
23
Consequences of release dispersion from an
urban university research facility
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Sample Results Obtained
  • Conclusions

24
Benefits of CFD Approach (1)
  • No scale-up problem
  • Three-dimensional, steady or transient
  • Interrogatable predictions
  • Handles effect of
  • blockages in domain
  • recirculating flow
  • multiple inlets and outlets
  • multiple interacting sources

25
Project 1 Emissions Dispersion Study
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Sample Results Obtained
  • Conclusions

26
3-D PLUME DISPERSION MODEL
  • Solution Domain
  • Solution domain encompasses the principal
    neighbouring buildings for at least one block on
    each side of the research facility
  • Domain 260m by 260m by 66m high

27
3-D PLUME DISPERSION MODEL
  • Solution Domain
  • PHOENICS VR object primitives used to represent
    building blockages, in the absence of CAD models
    to import
  • Some bespoke objects created e.g. for roofs)

28
CFD Model Description - 1
  • Representation of the effects of
  • blockage due to presence of neighbouring
    buildings, obstacles
  • resistance and mixing in tree canopy summer
    only
  • ambient wind vector and temperature profile
  • multiple interacting releases (chillers,
    laboratory extracts etc)

29
CFD Model Description - 2
  • Dependent variables solved for
  • pressure (total mass conservation)
  • axial, lateral and vertical velocity components
  • air / effluent mixture temperature
  • effluent concentration in mixture
  • turbulence kinetic energy
  • turbulence energy dissipation rate
  • Independent Variables
  • 3 spatial co-ordinates (x,y,z) and time

30
Roof-top Release Sites
  • Extract Stacks from Basement BSU
  • 2 off
  • Air Chiller Unit discharges
  • 12 off
  • Laboratory Extract Stacks
  • 8 off
  • Laboratory Discharge Stacks
  • 3 off

31
Overview of Release Conditions
32
Internal SourcesRooftop Release Specification
  • Basement Laboratory Extract Stacks
  • Two Vertical stacks
  • Stack diameter 0.95 m.
  • Height 3 m. above plant room roof
  • Release temperature - 24 deg.C
  • Release velocity - 15 m/s
  • Flowrate 2.84 m3/s each stack

33
Project 1 Emissions Dispersion Study
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Sample results Obtained
  • Conclusions

34
Environment Parameters Studied
  • Domain extent
  • extended down-wind domain
  • Ambient Wind
  • summer and winter wind directions
  • summer and winter temperature effects
  • Adjacent buildings
  • Influence of layout and topology
  • Environmental Factors
  • Tree canopy height, layout and resistance

35
Release Parameters Studied
  • Basement Extract Stacks
  • Release temperature - 24 deg.C
  • Release velocity - 15 m/s
  • Air chiller discharges
  • Release temperature - 24 deg.C
  • Release velocity - 2.6 m/s
  • BSX stack height
  • Reference - 3m. above chiller top
  • High - 6m. above chiller top
  • Also try - 9m. 12m. above chiller top

36
Ambient Parameters Studied
  • Summer
  • Ambient temperature - 24 deg.C
  • Wind from SW
  • Winter
  • Ambient temperature - 5 deg.C
  • Wind from NNE
  • Wind Speed (Pasquill D stability profile)
  • High - 8.0 m/s
  • Low - 2.5 m/s
  • Still - 0.5 m/s

37
Project 1 Emissions Dispersion Study
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations performed
  • Summary of findings
  • Conclusions

38
Summary of findings - 1
  • Under high wind conditions, from SW and NNE
    directions, plume trajectory is sufficient to
    clear neighbour buildings with stack at original
    elevation.
  • SW (summer) wind direction is worse than NNE
    (winter) direction.
  • Under low wind conditions, raising stack by 3 m.
    should be adequate

39
Summary of Findings - 2
  • Under still SW wind conditions, adjacent chiller
    discharge air curtains dominate flow pattern in
    vicinity of release.
  • BSX stack emission is entrained in complex flow
    pattern on roof, and dragged down to ground
    level. Flow reversal at low level spreads plume
    around side rear of building. Raising stack
    3m. alleviates, but does not eradicate, the
    problem.

40
Summer still wind flow patternOriginal Stack
location
41
Run 21 Summer still windOriginal Stack
location
42
Run 21 Summer still windOriginal Stack
location
43
Project 1 Emissions Dispersion Study
  • Industrial Context
  • Objectives of Study
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Summary of findings
  • Conclusions

44
Project 1 Dispersion Study Conclusions
  • Raising stack by 3m. would ensure adequate
    dispersion of plumes except under still, summer
    conditions.
  • However, in mitigation, . . . .
  • Is the predicted flow reversal at low level in
    the adjacent road a realistic scenario, or would
    occasional vehicular traffic in road be
    sufficient to prevent occurrence ?

45
Project 1 Dispersion Study Conclusions
  • Such very tall stacks were not an acceptable
    option
  • and so that
  • (for the time being)
  • was that.

46
Project 2
  • Dispersion Problem Diagnosis Remedy

47
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations performed
  • Synopsis of Results
  • Conclusions

48
Project 2Problem Definition - 1
  • The buildings of interest here are adjacent to
    the research facility building, whose proposed
    extension was the subject of the earlier
    emissions dispersion study.
  • The buildings, to be referred to as Building B
    and Building P are parallel to the road.
  • A linkage building forms an enclosed courtyard.

49
Overview of Site from South
50
Flow Geometry Close-up
51
Project 2Problem Definition - 2
  • Under adverse ambient conditions, traces of
    malodorous releases from laboratories in the
    Buildings B and / or P are apparently
    detectable at the upper floors on the courtyard
    side of the building linking the two . . . . .

52
Project 2Problem Definition - 3
  • Are the odorous releases originating from
    Building B, or Building P, or both ?
  • Do they indicate that there are hazardous
    dispersion consequences from these roof-top
    releases ?
  • If a hazard to the public exists, what is the
    extent, and how may it be eradicated ?

53
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations Performed
  • Synopsis of Results Obtained
  • Conclusions

54
Project 2Study Methodology
  • Use CFD simulations to predict plume trajectories
    issuing from rooftop extract release points on
    Buildings B P
  • Identify offending source(s)
  • Provide input to design of modified fume extract
    arrangements, to reduce impact by reducing
    effluent concentration at source

55
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations Performed
  • Synopsis of Results Obtained
  • Conclusions

56
Project 2Benefits of using CFD
  • Using concentration marker variables in CFD
    simulations allows identification of individual
    contributions to effluent concentrations at
    particular locations, as well as cumulative
    effects
  • Sources can be activated singly or together

57
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Synopsis of Results
  • Conclusions

58
Project 23-D Plume Investigation Model
  • Domain size - 250m by 400m by 60m .
  • Typical nodalisation level - 350,000
  • Target area is windows at upper level of link
    building, at 14.9m ASL
  • Problem will be worst in Winter , when wind is
    directed from sources to target. Summer
    prevailing wind is in opposite direction

59
Project 2Release Site Details
  • Building B Extract Arrangement
  • Vertical release from stack pipe
  • Release temperature - 24 deg.C
  • Release velocity - 10 m/s
  • Building P Extract Arrangement
  • Horizontal release ( N, S, E, W ) from capped
    vertical pipe
  • Release temperature - 24 deg.C
  • Release velocity - 3 m/s

60
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of simulations performed
  • Synopsis of Results Obtained
  • Conclusions

61
Project 2Outline of Simulations Performed
  • Simulations performed in 3 stages
  • Stage 1 - As is release concept both releases
    active still and low wind velocities
    summer and winter conditions
  • Stage 2 - Effect of single release, either from
    Building B or Building P
  • Stage 3 - Effect of revisions to release
    arrangements

62
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations Performed
  • Synopsis of Results
  • Conclusions

63
Project 2Findings of Stage 1 Study
  • Concentrations of effluent from releases are in
    excess of target level (lt 100 ppm) at courtyard
    walls
  • Winter conditions worse than summer
  • Low wind conditions worse than still wind
    conditions
  • This contrasts with the releases from the
    adjacent facility, which were worst under still,
    summer conditions)

64
Maximum Concentration of effluent at South wall
and at any wall in courtyard
65
Winter , Low WindBoth ReleasesEffluent
Spread Elevation 14.6m. asl
66
Project 2Objectives of Stage 2 Study
  • Thus far, have addressed simultaneous
  • as is emissions releases from the stacks
  • on Buildings B and P.
  • Now need to know
  • What is the contribution of each to the effluent
    levels in the courtyard ?

67
Stage 2 simulationsSummer, 0.5 m/s windPeak
effluent levels at courtyard walls
68
Stage 2 simulationsWinter, 2.5 m/s wind Peak
effluent levels at courtyard walls
69
Project 2Conclusions of Stage 2 Study
  • The effluent at the south face of the courtyard,
    where the problem has been reported, originates
    predominantly from the releases from Building P
    roof rather than from Building B roof.
  • More effective venting arrangements are required
    to remove the nuisance / hazard

70
Project 2Objectives of Stage 3 Study
  • Replace present horizontal outlet for Building
    P emissions by vertical discharge from stack at
    same elevation
  • Investigate possibility of reducing emissions
    from Building B by modifying stack discharge
    arrangements

71

Project 2 Stack modification options for
Building B - 1
  • Building B discharge stack is already at
    maximum permissible elevation
  • Try venturi sheath approach to dilute the
    effluent discharge with fresh ambient air prior
    to discharge
  • Implementation would not require major
    modification to existing arrangement

72
Project 2Venturi mixer design concept
  • A venturi-type stack discharge concept has no
    moving parts
  • It uses the momentum of the discharge jet to
    induce dilution mixing with the surrounding
    (free) ambient air flow

73
Project 2 Venturi Stack design parameters
  • Discharge pipe diameter
  • Discharge nozzle diameter
  • Venturi sheath bottom diameter
  • Venturi sheath top diameter
  • Venturi sheath length
  • Internal baffles ?

74
Principle of Venturi Discharge Stack
75
Venturi Stack Dispersion Results for Typical
Discharge Stack Geometry
76
Stage 3 Simulations Venturi Stack design
constraints
  • Total height not to exceed given limit
  • Discharge velocity not to exceed 15 m/s
  • Venturi sheath diameter limited by space
  • Fixed (high) effluent flowrate
  • Single Venturi sheath needed for each pipe

77
Stage 3 Simulations Venturi Stack design
constraints
  • The results obtained from using a venturi stack
    device represent a balance between the discharge
    velocity, the entrainment rate and the degree of
    mixing possible in the sheath
  • The constraints on the installation mean that
    effluent concentration levels at the point of
    discharge can only be reduced by a limited amount.

78

Project 2 Stack modification options for
Building P
  • Building P stack currently a 4-way horizontal
    discharge
  • Exposed and highly visible location rules out an
    elevated venturi sheath approach
  • Seek some improvement by adopting a vertical
    discharge arrangement

79
Project 2Dispersion Problem Diagnosis
Remedy
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Outline of Simulations Performed
  • Synopsis of Results
  • Conclusions

80
Project 2Conclusions of Project - 1
  • Emissions from the roof stacks of the two
    buildings can build up to significant levels in
    the courtyard between them
  • Build-up occurs over a variety of ambient
    conditions, being worse in winter and at higher
    wind speeds
  • Re-ingestion to the buildings could occur through
    windows which open onto the courtyard

81
Project 2Conclusions of Project - 2
  • Changing to a vertical release for the Building
    P releases, coupled with use of a venturi stack
    for the Building B releases, can reduce
    courtyard concentrations to acceptable levels
    under summer conditions.
  • This is the highest risk period when windows onto
    the courtyard are likely to be open for
    ventilation purposes

82
Project 2Conclusions of Project - 3
  • Concentrations of effluent from roof stack
    releases remain in excess of the recommended
    limit (100 ppm) in the courtyard under winter
    conditions.
  • In mitigation, windows giving onto the courtyard
    are then less likely to be open

83
Project 2Conclusions of Project - 4
  • Comparatively simple modifications to roof stack
    release arrangements can still result in
    significant reductions in effluent levels in the
    courtyard under winter conditions.

84
Project 2Conclusions of Project - 5
  • HOWEVER
  • If it were feasible to raise the stack on
    Building P a little (say 2 m.) above its
    present elevation, it might be possible to
    fit a short venturi nozzle.
  • In which case . . . . .

85
Winter, 2.5 m/s wind extended stack venturi
Peak effluent levels at courtyard walls
86
Project 2Conclusions of Project - 6
  • IN SHORT . . .
  • Effluent release concentrations at the upper
    courtyard levels could be dropped to acceptable
    levels of around 1104 dilution in winter
  • BUT ONE WAS NOT ALLOWED
  • TO RAISE THE STACK
  • BY THE NECESSARY 2 METRES . . .

87
Project 2Conclusions of Project - 7
  • AND SO THERE
  • FOR THE PRESENT
  • THE MATTER RESTED

88
Project 3
  • A
  • COMPARE AND CONTRAST
  • PROJECT

89
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

90
Project 3Problem Definition - 1
  • The two earlier projects had a common thread
  • Acceptable dilution dispersion of releases could
    be achieved under worst case ambient conditions
    only when the stack height was raised beyond an
    acceptable level .

91
Project 3Problem Definition - 2
  • Some alleviation could be achieved by dilution at
    point of release using a venturi device to
    entrain surrounding air
  • Unfortunately the ability of this concept to make
    real savings is limited by design constraints,
    most usually
  • height impairs mixing efficiency
  • nozzle velocity noise limits entrainment

92
Project 3Problem Definition - 3
  • Previous Flowsolve attention to venturi stacks
    has been conditioned by simplicity
  • free entrained air for dilution
  • no moving parts
  • but as we have seen, it has its limitations.
  • Meanwhile problems go unresolved

93
Project 3Problem Definition - 4
  • Now we have a possible solution
  • The Tri-Fan stack from
  • STROBIC AIR CORPORATION

94
Project 3Problem Definition - 5
  • This device combines
  • a mixing plenum, through which ambient air is
    drawn by a fan to dilute the fume stream
  • two venturi nozzles, through which the mixture is
    then forced
  • these 2 jets are then mixed, to induce
    entrainment of external air
  • two separate entrainment zones

95
Overview of Strobic Tri-Stack
96
Overview of Strobic Tri-Stack
97
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Benefits of using CFD
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

98
Project 2Study Methodology - 1
  • Use CFD simulations to predict plume trajectories
    issuing from rooftop extract release points on
    the original research building of Project 1
  • Compare and contrast the dispersion efficiency,
    under identical adverse weather conditions, of
    the Tri-Stack arrangement, and two vertical stack
    arrangements

99
Project 2Study Methodology - 2
  • The Contenders
  • Strobic Tri-Stack
  • Discharges at 21.75 m elevation
  • Original Throttled Stack
  • Discharges at 22.9 m elevation
  • Raised Throttled Stack
  • Discharges at 25.9 m elevation

100
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Reference Case Definition
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

101
Project 2Reference Case Definition - 1
  • Dispersion of Basement Extract fumes from stacks
    located at front of research facility
  • Worst case wind vector scenario from earlier
    study, to give tough case for comparison
  • Downwind plume trajectory passes directly over
    adjacent buildings

102
Project 2Reference case Definition - 2
  • Ambient Wind Vector Specification
  • Still wind in summer
  • Wind speed 0.5 m/s
  • Wind direction - from release directly over
    Buildings B and P downwind
  • Air temperature 28 0C

103
Project 2Reference case Definition - 3
  • Release Scenario
  • 6 m3/s effluent gas entering each stack via a 1m
    diameter duct
  • Vertical straight stacks throttled to give 15
    m/s exit velocity
  • Release temperature 24 0C

104
Project 2Reference case Definition - 4
  • Tri-Stack Operating Data
  • 6 m3/s effluent gas inlet feed
  • 6.75 m3/s plenum air feed
  • 15.69 m3/s entrained ambient air
  • 29.39 m/s nozzle velocity
  • Release temperature 24 0C

105
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Reference Case Description
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

106
Project 3CFD Model Details
  • 3-D PLUME DISPERSION MODEL
  • As described in earlier study (Project 1)
  • Solution domain 400 x 300 x 120 m high
  • Tri-Stack represented as discrete distributed
    sources internal details of plenum, fan and
    entrainment cap not solved for

107
Tri-Stack Discharge Arrangement
108
Original Stack Discharge Arrangement
109
Original Stack Discharge Arrangement
110
Raised Stack Discharge Arrangement
111
Raised Stack Discharge Arrangement
112
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Reference Case Description
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

113
Discharge Strategy Comparison
  • Comparison of 100ppm
  • plume core envelopes

114
100 ppm core envelopeOriginal Stack
115
100 ppm core envelopeRaised Stack
116
100 ppm core envelopeStrobic Tri-Stack
117
100 ppm core envelopeStrobic Tri-Stack
118
Discharge Strategy Comparison
  • Comparison of effluent
  • concentrations on adjacent surfaces

119
Effluent concentrations on surrounding
structures Original Stack
120
Effluent concentrations on surrounding
structures Raised Stack
121
Effluent concentrations on surrounding
structuresStrobic Tri-Stack
122
Discharge Strategy Comparison
  • Comparison of plume
  • cross-sections at vertical slices through release
    plane

123
Comparison of 1000ppm plume sections
124
Comparison of 5000ppm plume sections
125
Comparison of 20,000ppm plume sections
126
Discharge Strategy Comparison
  • Comparison of plume
  • cross-sections at horizontal slices at various
    elevations

127
1000 ppm contour sections at elevation 27m
128
1000 ppm contour sections at elevation 46m
129
1000 ppm contour sections at elevation 61m
130
Project 3Compare Contrast Discharge
Strategies
  • Problem Definition
  • Study Methodology
  • Reference Case Description
  • Description of CFD Model
  • Summary of Results Obtained
  • Conclusions

131
Project 3Conclusions of Project - 1
  • The forced induction and additional dilution of
    the effluent at the point of release, which are
    afforded by the Tri-Stack device, give rise to
    clearly better dilution dispersion under the
    extreme conditions of the test case than can be
    obtained from the original or 3m-extended
    ordinary stacks

132
Project 3Conclusions of Project - 2
  • The Tri-Stack would appear to offer great
    advantages over throttled or natural
    venturi-enhanced systems when stack heights are
    limited by planning or aesthetic constraints

133
Lest we forget ..
  • Our thanks to
  • David Glynn Flowsolve
  • John Gibson Scott Wilson
  • Phil Milne-Smith Critical Airflow Controls
  • Paul Tetley Strobic Air Corporation
  • and not forgetting
  • the University Authorities

134
Thank you for your attention
  • Thats
  • all
  • for
  • now
  • ...
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