Carl Cressey

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  • 8/9/2019 Carl Cressey

    1/44

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    M

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    72-0- 89 :2- 2-/: ;9/8. >-015/; ?5:12-= 19>- @09>A  

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  • 8/9/2019 Carl Cressey

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Qvc CRITICAL ZONE 

    Qve = Building Codes No

    Qve = U.L. Values No

    Qve = Qvc x H eff Yes 

    (heat load x hood efficiency)

    O#?@*)#D"% !=@E*7? (*) P=@=)+#$#$G 4CE"A?@ 3"@=?

    Qvc = Output of Cooking

    Equipment X

    VmAn o@!=Vk 4kkK@ee?ma =@4! a4?m !V

    !=@ 7?!6=@m3

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    PQ R+, '%"' S$3'3(3Q

    Measures minimum exhaust air flow rate based on 400° F,

    600° F and 700° F (solid fuel).

    30% fat burgers are placed on a 21/2 sq.ft. appliance

    located on the end of the hood.

    The burgers are cooked at the prescribed surface

    temperature and flipped.

    The U.L. inspector observes the capture & containment of

    visible cooking vapors.

    The test was not established to measure hood efficiency orheat gain to the space.

    [

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3 ASTM F 2474 HEAT GAIN CURVEGENERIC EXAMPLE  

    @H8#.', "#,$'

    =$#,

    a#1+

    ,35@4,2>@4  $;A>;52

    CAPTURE &CONTAINMENT

     

    6#*,."1+Fe*1))1+F

    OW

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    FULL C&C OFCONVECTIVE HEAT

    (Appliance : 600°F) 

    HEAT SPILLING (airflowslowered below C&C threshold)

    (Appliance : 600°F)

    •  91'.#)1B$' 08#+F$' 1+ #1" /$+'1,;

    •  o&"$ '$+'1:5$ ,8#+ 51'.#)1B1+F '%&S$

    • 

    R.10S); '$$ 1%*#0, &- /$'1F+ 08#+F$'

    Schlieren Thermal

    Imaging  

    OO

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    600 °F SURFACE TEMP., FULL C&COF CONVECTIVE HEAT

    SAME APPLIANCE, CONVECTIVEHEAT SPILLING

    Measuring hood efficiency using CFD Technology  

    O="@

    5H#%%#$G

    Heat load design = High Efficiency  O="@

    ,"H@A)=7

    ON

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    *-B (- $)&C0) *--& 4DE%CF( ;'GH-BI

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    4**)1#+0$ *&'1:&+ 1+ S1,08$+

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    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

     A B C D

    System configuration

       A  n  n  u  a   l  e  n  e  r  g  y  c  o  s   t  s ,

       $

    #+/ ,;*$ &- 8&&/ 0#+ 1%*#0, #1"I&EF"$#,);3

    OU

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    According to the University of Minnesota (Gerstler, et. al, 1998) grease is comprised of

    a variety of compounds including solid and/or liquid grease particles, grease and water

    vapors, and a variety of non-condensable gases including nitrogen oxides, carbon

    dioxide, and carbon monoxide. The composition of grease becomes more complex toquantify as grease vapors may cool down in the exhaust stream and condense into

    grease particles. In addition to these compounds, hydrocarbons can also be generated

    during the cooking process and are defined by several different terminologies including

    VOC (volatile organic compounds), SVOC (semi-volatile organic compounds), ROC

    (reactive organic compounds), and many other categories.

    ]8#, 1' a"$#'$l

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3OP

    =&E 1' F"$#'$ %$#'."$/lll

    4e!o MUO[

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    =&E 1' a"$#'$ R.#+:Y$/l

    !&,#) a"$#'$ @%1''1&+' D; 4**)1#+0$6#,$F&";

    OX

    0

    10

    20

    30

    40

    50

    60

       G   a   s   G   r   i   d   d   l   e

       E   l   e   c   t   r   i   c

       G   r   i   d   d   l   e

       G   a   s   F   r  y   e   r

       E   l   e   c   t   r   i   c

       F   r  y   e   r

       G   a   s   B   r   o   i   l   e   r

       H   a   m   b  u   r   g   e   r

       E   l   e   c   t   r   i   c

       B   r   o   i   l   e   r

       H   a   m   b  u   r   g   e   r

       G   a   s   B   r   o   i   l   e   r

       C   h   i   c   k   e   n

       E   l   e   c   t   r   i   c

       B   r   o   i   l   e   r

       C   h   i   c   k   e   n

       G   a   s   O  v   e   n

       E   l   e   c   t   r   i   c

       O  v   e   n

    Cooking Operation

       T   o   t   a   l

       G   r   e   a   s   e   E   m   i   s   s   i   o   n   s   (   l   b .   /   1   0   0   0   l   b .   )

    Total Emissions (lb./1000 lb. product)

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    010

    20

    30

    40

    50

    60

    70

    80

    90

    100

       G  a  s   G  r   i   d   d   l  e

       E   l  e  c   t  r   i  c

       G  r   i   d   d   l  e

       G  a  s   F  r  y  e  r

       E   l  e  c   t  r   i  c

       F  r  y  e  r

       G  a  s   B  r  o   i   l  e  r

       H  a  m   b  u  r  g  e  r

       E   l  e  c   t  r   i  c

       B  r  o   i   l  e  r

       H  a  m   b  u  r  g  e  r

       G  a  s   B  r  o   i   l  e  r

       C   h   i  c   k  e  n

       E   l  e  c   t  r   i  c

       B  r  o   i   l  e  r

       C   h   i  c   k  e  n

       G  a  s   O  v  e  n

       E   l  e  c   t  r   i  c

       O  v  e  n

    Cooking Operation

       %

       G  r  e  a  s  e   C  o  m  p  o  s   i

       t   i  o  n

    % Particulate % Vapor 

    C#":0)$ #+/ 5#*&" F"$#'$ *$"0$+,#F$' D;

    #**)1#+0$ 0#,$F&";

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    0

    10

    20

    30

    40

    5060

    70

    80

    90

    100

       G  a  s   G  r   i   d   d   l  e

       E   l  e  c   t  r   i  c

       G  r   i   d   d   l  e

       G  a  s   F  r  y  e  r

       E   l  e  c   t  r   i  c

       F  r  y  e  r

       G  a  s   B  r  o   i   l  e  r

       H  a  m   b  u  r  g  e  r

       E   l  e  c   t  r   i  c

       B  r  o   i   l  e  r

       H  a  m   b  u  r  g  e  r

       G  a  s   B  r  o   i   l  e  r

       C   h   i  c   k  e  n

       E   l  e  c   t  r   i  c

       B  r  o   i   l  e  r

       C   h   i  c   k  e  n

       G  a  s   O  v  e  n

       E   l  e  c   t  r   i  c

       O  v  e  n

    Cooking Operation

       %

       G  r  e  a  s  e   C  o  m

      p  o  s   i   t   i  o  n

    % PM 2.5 % > PM 2.5 and PM 10

    C#":0)$ '1B$ /1',"1D.:&+ D; 0&&S1+F *"&0$''

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Filter Efficiency Comparison @ 196 cfm/ft

    0.0

    10.0

    20.0

    30.0

    40.0

    50.0

    60.0

    70.0

    80.0

    90.0

    100.0

    0.0 2.0 4.0 6.0 8.0 10.0 12.0Particle Size (micron)

       P  a  r   t   i  c  u   l  a   t  e   R  e  m  o  v  a   l   E   f   f   i  c   i  e  n  c  y   (   %   )

    Standard KSA Aluminum Baffle Cartridge Filter Baffle 2

     [N_ ,& [X_

    $Z01$+,

    &+ *#":0)$'

    D$,E$$+ U

    #+/ OW %10"&+'

    E1,8 81F8 $Z01$+0;Y),$"'

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    !8$"$ 1' # oV! -&" /$,$"%1+#:&+ &- $t.$+, "$)$#'$/

    K$'.),' /1u$" -&" /1u$"$+, #**)1#+0$' J$5$+ E1,81+ '#%$ F"&.*'Q

    #+/ %$/1.%' JY'8< 0810S$+< D$$-Q 1i$i< $t.$+, 1' 81F8); *"&0$''/$*$+/$+,

    j  e1F+1Y0#+, )$5$)' &- F"$#'$ 5#*&" #"$ *"$'$+, 1+ 0&&S1+F $t.$+,

    o#; 5#"; -"&% NW_>[W_ D; %#''

    ?%*)10#:&+' -&" ,;*$ &- F"$#'$ "$%&5#) /$510$

    C#":0)$' )$'' ,8#+ Co OW #"$ +&, $#'1); "$%&5$/ D; ,"#/1:&+#)

    1+$":#) %$,8&/'

    C&'$ %.08 81F8$" "1'S ,& 8.%#+ 8$#),8

    e.%%#";g

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    How Is UV Applied On 

    Emissions?  

    UV Light for destruction

    of grease

    MN

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Photolysis

    Long chain molecules are brokendown into shorter chains.

    "  Double bonds are destroyed into the long-chain

    VOC molecules

    The cooking effluent is exposedto UV light.

    "  Air, water vapor and VOCs are exposed to UV-C light

    !  This process called “PHOTOLYSIS” addsenergy to the molecular chains, which breaksbonds and creates radicals. 

    Step 1 MT

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Ozonolysis

    -

    +-

    +

      -

       +

    +-

    +

    +

    +

    -

    -

    + -

    +

    1. 

    Exposure to UV-C light adds an

    extra atom to Oxygen (O2)

    2. 

    This creates ozone (O3). 

    3. 

    Ozone connects to organic

    compounds in the exhaust air

    stream and converts them to H2O

    and CO2.

    4. 

    This reduces many odor containing

    compounds produced in thecooking process.

    Step 2 MU

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    7@ :%JKF '.F(%LL)& '. )DE%CF(

    KL).CJ

    o$08#+10#) $H,"#0,&"'< *"1%#"; #+/ '$0&+/#";

    D$-&"$ c9 )#%*'

    PTU( E/=8 ;5

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Filter samples from EPA Method 5 test

    Cooking hamburgers without and with UV light

    Without UVWith UV-C light

    EPA Method 5 testing with Western KY  

    University To Analyze Emissions 

    MP

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Grease build up

    on face of meshfilter.

    UV System eliminatedgrease deposition on back

    of mesh filters, plenum

    and duct system after 10

    months of operation.

    Filter Analysis 

    MX

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Exhaust duct directly after the

    Capture Ray plenum shows a powdery inert compound.

    Further downstream no

    evidence of the inert powder is present indicating the continuing

     presence of ozone.

    Condition Of The Duct  

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Photos From Ductwork And Inside The Hoods 

    Queen Mary II

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    Hood Damper With UV-System 

    Queen Mary II

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3

    • 

    Duct, Fan & Roof Cleaning Costs Reduced

    • 

    Converts Grease to Powder

    • 

     Alters Cooking Odors

    • 

    Extends Roof-Liner Life

    • 

    Reduces Risk of Fire

    Ultra-Violet Light Technology  

    6CJJ%GM

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    -Make-up air with mixing ventilation (CFD)

    72/: 5>F/1: 89-. :2- :HF- 9@ .GFF;H /50

    2/4- 9= 2998 F-0@90>/=1- /=8 .F/1-

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    NN

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    Mixing

    ventilation

    system

    requires15 to 20%

    higher

    exhaust rate

    than

    displacement

    system for the

    same

    efficiency.

    W/?-UGF /50 65:2 85.F;/1->-=: 4-=B;/B9= I(XYK

    NT

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    •  Low velocity thermal displacement

    assists in capture & containment of thecooking plume. Natural buoyancy of

    supply air helps “push” convective

    plume into the hood.

    •  High velocity mixing diffusers can

    disrupt the cooking plume, striking the

    face of the hood, forcing supply airdown the face and actually drawing heat

    away from the hood.

    DISPLACEMENT  MIXING

    "GFF;H /50 5>F/1:. 2998 F-0@90>/=1-Z

    NU

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    !"#$%&' #) *"$'$+,$ $) -.,."& /$ )# 0&+',".0012+3M.A.R.V.E.L. Demand ControlSystem

    DCV Exhaust regulation principle

    KITCHEN START UP

    > Fan is switched on> Cooking appliances are not yet powered

    KITCHEN START UP

    > Fan is ON, adjust continuously within idle range> Cooking appliances are warming up

    KITCHEN OPERATIONAL

    > Fan is ON> Cooking detected

    KITCHEN OPERATIONAL

    > Fan is ON

    > Full load cooking detected

        A    i   r    f    l   o   w     (

        C    F    M    )

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    VARIOUS COOKING OPERATIONS 

    => Cooking appliances which are in cooking mode are

    detected by the sensors

    => Dampers & fan are adjust between idle and maximumairflow

    Balancing Dampers forconnection of multiple hoodsto a common fan

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