Manual Flash Pasteurizacion

PROCESS & PACKAGING, INC. 5450 Tech Circle, Moorpark, CA 93021 Tel: (805) 529-9890 Fax: (805) 529-9282

OPERATION MANUAL

FLASH PASTEURIZATION

(FP & UFP SYSTEMS)

Keg cleaner, keg cleaning, Sankey keg, semi-automatic keg washing, sanitizing & filling, semi-automatic keg washing, sanitizing and filling, automatic keg washing, sanitizing & filling, semi-automatic keg washing, sanitizing and filling, stainless steel Sankey keg, American Sankey, European Sankey, Flash Pasteurizer, Flash Pasteurize, Flash Pasteurization, Brewing System, Brew House, Brewery, Micro Brewer, Keg Washer, Fill By Weight, Wine on Tap, Winemaker, Fill By Weight Keg Filling, Fill By Weight Beer, Fill By Weight Wine



PROCESS & PACKAGING, INC.

TABLE OF CONTENTS A

TITLE SECTION Table of contents A What is Pasteurization a Preface B Disclaimer C Confidentiality and Copyrights D Operational Safety Notes EMERGENCY STOP E Training F Specifications G Start-up and Shut-down Procedure H C.I.P. Procedures I Machine Layout J Electrical Section K Mechanical Section L Pneumatics Section M I/O List N Oxine O Planned Prevenative Maintenance Schedule P Dimensions R Spares S Services T Cycle Times V Flow Diagram W Control Philosophy X Appendix Section Z


PREFACE B The SYSTEM has been designed as a self contained and reliable automatic Flash Pasteurization system. The following instructions and information have been prepared to clarify operational and maintenance procedures and should ensure long, reliable service from the machine if followed carefully. Proper maintenance and use of approved spare parts will extend the life of the system and it's reliability. The use of any non approved spare parts may void any warrants or guarantees, actual or implied.

DISCLAIMER C The customer assumes all responsibility for the SYSTEM once delivered. The SYSTEM is tried and tested equipment. As such IDD Processing & Packaging will not be held responsible for alterations and modifications carried out by the customer without the written approval of IDD Processing & Packaging.

CONFIDENTIALITY & COPYRIGHT D All information within is confidential and the copyright of IDD Process & Packaging, Inc. No portion of this data shall be released, disclosed, used or duplicated for use in procurement or manufacturing without the express written permission from IDD Process & Packaging, Inc.


OPERATIONAL SAFETY NOTES E WEAR SAFETY GOGGLES Wear Safety Goggles approved for use by your Safety and Operational Procedures Committees when operating or observing this system. WEAR CHEMICAL-RESISTANT GLOVES Wear Chemical-Resistant Gloves approved for use by your Safety and Operational Procedures Committees. WEAR BACK SUPPORT EQUIPMENT Wear Back Support Equipment approved for use by your Safety and Operational Procedures Committees and use proper lifting technique approved for use by your Safety and Operational Procedures Committees. VENTILATION Area should have adequate ventilation approved for use by your Safety and Operational Procedures Committees. Respirators should be used during cleaning and operations where fumes are present.

EMERGENCY STOP MANUAL STOP In an emergency use the RED mushroom button to isolate the power and stop the process sequence at any time. The Emergency Stop Button is located on the Main Control Panel.


TRAINING F . On-site training is available from our technical staff at the customers request.

SPECIFICATIONS G Output parameters. Note: Insert your specific optimum and acceptable values into this chart for your internal reference. This chart is the be used as a bench mark in the future of your production. Change in operating personnel, valves, wash sequences and mechanical integrity can be tracked with this bench-marking.

Date: Temperatures: Chase Times: Flow Rate: Special Notes:

PROCESS & PACKAGING, INC. 1999

START UP AND SHUT DOWN PROCEDURES H

SEE CONTROL PHILOSOPHY SECTION FOR DETAILS


C.I.P. PROCEDURES I

See the 'Control Philosophy' section and the following notes to suit the

specific plant requirements


MACHINE LAYOUT J


ELECTRICAL SECTION K

PLEASE NOTE:

Customer to supply local disconnect and ground fault device


MECHANICAL SECTION L

SEE SUPPLEMENTAL TECHNICAL DATA MANUAL

FOR ADDITIONAL INFORMATION IF PROVIDED

BUTTERFLY VALVES

F.lli TASSALINI s.p.a.

F.lli TASSALINI S.p.A. BUTTERFLY VALVES

Page 1

Application Butterfly valves are universal and economical on/off routing valves

used for isolation and control in food processing pipelines. Features They are sanitary valves that offer low flow resistance and

reversible flow direction providing gentle treatment of product.

Valve maintenance is easy and valves have long service life.

All flanges with the same diameter are interchangeable thus allowing any combination of outlets as well as combinations between different standards. Valves can be operated manually or pneumatically. Manual valves are available with a wide choice of handles that lock in intermediate positions, so that the flowrate can be regulated. Pneumatic valves are available with a full range of accessories, including horizontal and vertical single-, double-acting and flow control actuators, control tops and electrical components. All handles and actuators are fitted onto the valve with the same connection. This allows for great flexibility and increased savings during extensions or modifications of processing lines.

Components

PARTS LIST

1 Butterfly Aisi 316L 2 Seal Silicone, EPDM, FTM, PTFE-coated FTM, PTFE + silicone 3 Screw Aisi 304L 4 Flange Aisi 304L/Aisi 316L 11 Bush PTFE


Page 2

Technical Data Max. product pressure: 700 kPa (7 bar); for valves with PTFE seals

max 200 kPa (2 bar). Recommended working pressure: 600 kPa (6 bar). General temperature range: -10C +95C (+15F +205F).

Seals temperature range:

! silicone: -50C +200C (-60F +390F); ! EPDM: -30C +140C (-20F +280F); ! FTM: -15C +220C (+5F +430F); ! PTFE-coated FTM: -10C +150C (+15F +300F); ! PTFE + silicone: -10C +150C (+15F +300F).

Finish: 120 grit (max Ra 1.01-1.14 m, 40-45 ). Production range:

! manual butterfly valves from DN 10 to DN 250 and to 10;

! pneumatic butterfly valves from DN 25 to DN 100 and 1 to 4.

Connections: welding end, expanding end, threaded end, liner + nut, bend, flange, ferrule end. Standards: DIN, SMS, RJT BS, IDF ISS, BSP, Eno, Macon, Clamp. Steel grades: Aisi 304L, Aisi 316L.

Torque Ratings Butterfly valves with silicone seal:

DIAMETER OPEN [90] CLOSE [0]

1 1 NW 5 NW 1 1 NW 5 NW 2 2 NW 17 NW

2 5 NW 28 NW 3 6 NW 32 NW


Page 3

p

(kPa

)

Flowrate Q = m3/h

p

(kPa

)

Flowrate Q = m3/h

Pressure Drop Butterfly valves DIN: Butterfly valves SMS, RJT BS, IDF ISS, Clamp:

For further technical information, section and dimensional drawings and range of models available please refer to our series of product brochures, technical catalogues and valve manuals.

API Schmidt-Bretten Plate Heat Exchangers

Plate Pack Arrangement

Contract Number: NP111012-101 Document Number: 4-026-GBF-086-001.PA

Plate Grouping: SECT 1 1/1*3SH Left Side (Beer)HEATING 1/1*3SH Right Side (Water)SECT 2 8/8*4SH Left Side (Beer)REGEN 8/6*4SH+2*4SW Right Side (Beer)

` SECT 3 1/1*7SH Left Side (PG 25%)COOLING 2/2*3SH Right Side (Beer)

Plate Summary: Part Number Qty Plate Pack Dimension:3-026-B5HM-00F23 13-026-B6HM-00F01 5 22.423 inches Maximum3-026-B6HM-00F02 5 21.756 inches Minimum3-026-B5HM-00F03 483-026-B6HM-00F04 13-026-B6HM-00F05 33-026-B6HM-00F06 33-026-B6HM-00F11 63-026-B6HM-00F12 53-026-B6HM-00F16 13-026-B6HM-00F26 13-026-B6HM-00F29 13-026-B5WM-00F03 43-026-B6WM-00F05 13-026-B6WM-00F06 1

86 Total

Arrangement: Plate No. Part Number Figure Gaskets face fixed head.

1 3-026-B5HM-00F23 R ACR/ECR2 3-026-B5HM-00F03 L CL3 3-026-B5HM-00F03 R CR4 3-026-B5HM-00F03 L CL5 3-026-B5HM-00F03 R CR6 3-026-B6HM-00F04 L DL7 3-026-B6HM-00F16 R PR

INTERMEDIATE GRID8 3-026-B6HM-00F26 L AFL/EFL9 3-026-B6HM-00F12 R KR10 3-026-B5HM-00F03 L CL11 3-026-B5HM-00F03 R CR12 3-026-B5HM-00F03 L CL13 3-026-B5HM-00F03 R CR14 3-026-B5HM-00F03 L CL15 3-026-B5HM-00F03 R CR16 3-026-B6HM-00F02 L BL17 3-026-B6HM-00F05 R FR18 3-026-B6HM-00F11 L KL19 3-026-B5HM-00F03 R CR

Page 1 of 3



20 3-026-B5HM-00F03 L CL21 3-026-B5HM-00F03 R CR22 3-026-B5HM-00F03 L CL23 3-026-B5HM-00F03 R CR24 3-026-B6HM-00F01 L AL25 3-026-B6HM-00F06 R ER26 3-026-B6HM-00F12 L LL27 3-026-B5HM-00F03 R CR28 3-026-B5HM-00F03 L CL29 3-026-B5HM-00F03 R CR30 3-026-B5HM-00F03 L CL31 3-026-B5HM-00F03 R CR32 3-026-B6HM-00F02 L BL33 3-026-B6HM-00F05 R FR34 3-026-B6HM-00F11 L KL35 3-026-B5HM-00F03 R CR36 3-026-B5HM-00F03 L CL37 3-026-B5HM-00F03 R CR38 3-026-B5HM-00F03 L CL39 3-026-B5HM-00F03 R CR40 3-026-B6HM-00F01 L AL41 3-026-B6HM-00F06 R ER42 3-026-B6HM-00F12 L LL43 3-026-B5HM-00F03 R CR44 3-026-B5HM-00F03 L CL45 3-026-B5HM-00F03 R CR46 3-026-B5HM-00F03 L CL47 3-026-B5HM-00F03 R CR48 3-026-B6HM-00F02 L BL49 3-026-B6HM-00F05 R FR50 3-026-B6HM-00F11 L KL51 3-026-B5HM-00F03 R CR52 3-026-B5HM-00F03 L CL53 3-026-B5HM-00F03 R CR54 3-026-B5HM-00F03 L CL55 3-026-B5HM-00F03 R CR56 3-026-B6HM-00F01 L AL57 3-026-B6HM-00F06 R ER58 3-026-B6HM-00F12 L LL59 3-026-B5HM-00F03 R CR60 3-026-B5WM-00F03 L CL61 3-026-B5HM-00F03 R CR62 3-026-B5WM-00F03 L CL63 3-026-B5HM-00F03 R CR64 3-026-B6HM-00F02 L BL65 3-026-B6WM-00F05 R FR66 3-026-B6HM-00F11 L KL67 3-026-B5HM-00F03 R CR68 3-026-B5WM-00F03 L CL69 3-026-B5HM-00F03 R CR70 3-026-B5WM-00F03 L CL

Page 2 of 3



71 3-026-B6HM-00F01 R BR72 3-026-B6WM-00F06 L FL

INTERMEDIATE GRID73 3-026-B6HM-00F29 R AJR/EJR74 3-026-B6HM-00F11 L KL75 3-026-B5HM-00F03 R CR76 3-026-B5HM-00F03 L CL77 3-026-B5HM-00F03 R CR78 3-026-B5HM-00F03 L CL79 3-026-B6HM-00F02 R AR80 3-026-B6HM-00F12 L LL81 3-026-B5HM-00F03 R CR82 3-026-B5HM-00F03 L CL83 3-026-B5HM-00F03 R CR84 3-026-B5HM-00F03 L CL85 3-026-B6HM-00F01 R BR86 3-026-B6HM-00F11 L KL

Page 3 of 3

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SERIE 201LKD

MOD.200 LKD

CODICEGRUPPO

Disegnato

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Materiale

Revisione

ControllatoPeso

S.p.

A.ZO

RZIN

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Ai sensi delle vigenti leggi, la Zorzini spa si riserva la propiet di questo disegno con il divieto di riprodurlo e/o renderlo notoa terzi senza autorizzazione

26/04/2007

ISO

TOLLERANZE OVE NON INDICATE

SECONDO ISO-2768 CL.-C- (grossolana)

0,2 0,3 0,5 0,8 1,2 2 3 4

da

fino a fino a fino a fino a fino a fino a fino a fino a

da da da da da da da

0,5

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3 6 30 120 400 1000 4000

6 30 120 400 1000 2000 4000

1:5 14404-14301

5352

3

9

579A

A

SEZIONE A-A

1

0

0

12

20M

4

7

2

9

11

10

8

6

5

31

11 95020 VITE TCEI M10X20 A2 2

10 95423 ANELLO ELAST. D18,5 A2 1

9 94042 VOLANTINO VI/190 AISI 304 1

8 97062 RONDELLA 44X20 SP 3 NYLON 17 71085 TRAVERSINO 1

6 97210 BUSSOLA PER SNODO AISI304 1

5 97285 SNODO AISI 304 1

4 71017 BRACCIO 1

3 9604 GUARNIZIONE G/200LKD V.MESCOLE 1

2 7CA0801 COPERCHIO 200LKD 1

1 7TA0802 TELAIO C/SUPP. 1

Pos N doc. Descrizione Materiale Q.t note

4

3

5

VARIANTIP. MAX (bar) MESCOLE

4,8 NBREPDM

SILICONEFPM

27,4

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26/04/2007

Ai sensi delle vigenti leggi, la Zorzini spa si riserva la propiet di questo disegno con il divieto di riprodurlo e/o renderlo notoa terzi senza autorizzazione

ZORZ

INIS.

p.A.

Peso

Controllato

Revisione

Materiale

ORSARIA

Scala

Disegnato

GRUPPOCODICE

PORTELLA 180

SERIE 180

TITOLONOME DATA Firma

FA04 0



0,2 0,3 0,5 0,8 1,2 2 3 4

da



0,5

3

3 6 30 120 400 1000 4000

6 30 120 400 1000 2000 4000

A

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SEZIONE A-A498

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3

4

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1

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SP

457

440

3

6 2

4

8

5

7

91

9 9621 GUARNIZIONE G/170 V.MESCOLE 1

8 94053 VOLANT. MEC/90 M16 1

7 97008 RONDELLA 16X30 14404-EN10028-7 16 71080 TRAVERSINO AISI 304 1

5 95421 ANELLO ELAS.10 A2 14 93012 SPINA TESTA TORNITA AISI 304 1

3 71031 BRACCIO 1

2 7CA0400 COPERCHIO FINITO 1

1 7TA0400 TELAIO C/SUPPORTI 1


VARIANTIH H1 SP SP 2 P. MAX (bar) MESCOLE60 166 6 1,5 1,3 NBR80 186 6 1,5 1,3 EPDM60 166 8 2 1,3 SILICONE80 186 8 2 1,3 FPM

26/04/2007

Ai sensi delle vigenti leggi, la Zorzini srl si riserva la propriet di questo disegno con il divieto di riprodurlo

Z

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Scala

Disegnato

GRUPPOCODICE

Ind. Modifica

PORTELLA 165

SERIE 165

TITOLONOME DATA Firma

FA27 01:5

A

A

SEZIONE A-A

14404-14301

12 2

9

13

7

11

4

6

8

5

10

14

3

1

14 97257 TUBO DIST. L=123 AISI 304 1

13 91030 TIRANTE M12X166 AISI 304 1

12 71005 BRACCIO di CHIUSURA 1

11 94031 VOL. VI165A C/CODOLO AISI 304 1

10 97044 RONDELLA 34 SP 3 19 91009 TIRANTE M16 L=120 14301/7-EN10028-7 1

8 95421 ANELLO ELAS.10 A2 27 93006 SPINA 12X30 AISI 304 26 95210 DADO CIECO M12 A2 2

5 97031 RONDELLA M12 GROWER A2 ARM. 2

4 95031 VITE TE M12X50 A2 1

3 9620 GUARNIZIONE G/R165 V.MESCOLE 1

2 7CA2700 COPERCHIO FINITO 1

1 7TA2700 TELAIO C/SUPPORTI 1




0,2 0,3 0,5 0,8 1,2 2 3 4

da



0,5

3

3 6 30 120 400 1000 4000

6 30 120 400 1000 2000 4000

12,8

NOTEP. MAX (bar) MESCOLE

0,5 NBREPDM

SILICONEFPM

6

0

8

2

332440

547

1

8

0

3

4

5

452

Materiale I Temperatura I PesoMoteriol I Temperature lWeight

ffiffiffireffire

Guarn iz ioneGosketMontaggio sul coperchio, senza cnllanteFixed on the cover, without glue

Guarn iz ioneGosketMontaggio sul coperchio, senza collanteFixed on the cover, without glue

Guarn iz ioneGosketMontaggio sul coperchio, senza cnllanteFixed on the cover, without glue


Guarniz ioneGosketMontaggio sul coperchio, con collanteFixed on the coven with glue

=N

Guarn iz ioneGoskefMontaggio sul coperchio, senza collanteFixed on the cover, without glue


Guarn iz ioneGosketMontaggio sul coperchio, con collanteFixed on the cover, with glue

Temperatura,Temperoture

ffiffiffiffiffiffi

Peso kgWeight lq

Guarn iz ioneGosketMontaggio sul coperchio, con collanteFixed on the cover, with glue

=H

GOULDS PUMPSCommercial Water

28

Dimensions and Weights 5SV Series 3500 RPM

Motor Dimensions (in) Weight (lbs.)

NEMA Frame L2 D1 (max.) Motor Pump/Motor

Pump HP ODP TEFC ODP TEFC L1 ODP TEFC ODP TEFC L3 L4 L5 L6 M ODP TEFC ODP TEFC D2 Pump ODP TEFC ODP TEFC ODP TEFC ODP TEFC Type 1 1 3 3 1 1 3 3 (Ref.) 1 1 3 3 1 1 3 3 1 1 3 3

5SV-02 0.75 12.85 10.79 9.91 9.16 9.29 - - 9.57 9.57 5.19 6.20 6.19 6.19 6.19 4.13 27 21 21 19 19 48 48 46 46

5SV-03 1 13.84 10.66 11.19 9.16 9.29 - - 10.55 10.55 5.19 6.19 6.19 6.19 6.19 4.13 28 27 29 21 21 55 57 49 49

5SV-04 1.5

14.82 10.67 11.19 10.66 9.91 - - 11.54 11.54 5.74 6.20 7.19 6.19 6.19 4.13 30 32 40 23 23 62 70 53 53

5SV-05 15.8 10.67 11.19 10.66 9.91 - - 12.91 12.91 5.74 6.20 7.19 6.19 6.19 4.13 32 32 40 23 23 64 72 55 55

5SV-06 2 56C 16.78 11.18 12.06 11.16 10.79 - - 13.9 13.9 5.74 7.19 7.19 6.20 6.19 4.72 33 43 51 32 33 76 84 65 66

5SV-07 17.77 11.18 12.06 11.16 10.79 15.87 9.53 14.88 14.88 5.74 7.19 7.19 6.20 6.19 4.72 35 43 51 32 33 78 86 67 68

5SV-08 18.75 11.57 13.44 11.18 11.16 16.85 10.51 15.87 15.87 5.75 6.50 7.19 7.16 7.19 5.51 35 49 64 41 44 84 99 76 79

5SV-09 3 19.73 11.57 13.44 11.18 11.16 18.23 11.5 17.24 17.24 5.75 6.50 7.19 7.16 7.19 5.51 37 49 64 41 44 86 101 78 81

5SV-10 20.71 11.57 13.44 11.18 11.16 19.21 12.48 18.23 18.23 5.75 6.50 7.19 7.16 7.19 5.51 37 49 64 41 44 86 101 78 81

5SV-11 22.45 13.93 15.43 12.55 13.93 20.2 13.46 19.21 19.21 6.87 8.88 8.86 9.02 8.86 5.51 41 81 92 62 69 122 133 103 110

5SV-12 23.43 13.93 15.43 12.55 13.93 21.18 14.45 20.2 20.2 6.87 8.88 8.86 9.02 8.86 5.51 42 81 92 62 69 123 134 104 111

5SV-13 24.42 13.93 15.43 12.55 13.93 22.17 15.43 21.18 21.18 6.87 8.88 8.86 9.02 8.86 5.51 44 81 92 62 69 125 136 106 113

5SV-14 5 184TC 182TC 25.4 13.93 15.43 12.55 13.93 23.15 16.42 22.17 22.17 6.87 8.88 8.86 9.02 8.86 5.51 45 81 92 62 69 126 137 107 114

5SV-15 26.38 13.93 15.43 12.55 13.93 24.13 17.4 23.15 23.15 6.87 8.88 8.86 9.02 8.86 5.51 46 81 92 62 69 127 138 108 115

5SV-16 27.37 13.93 15.43 12.55 13.93 25.12 18.39 24.13 24.13 6.87 8.88 8.86 9.02 8.86 5.51 47 81 92 62 69 128 139 109 116

5SV-17 184TC 28.55 13.93 15.43 12.55 13.93 26.1 19.37 25.11 25.11 6.87 8.88 8.86 9.02 8.86 5.51 49 81 92 62 69 130 141 111 118

5SV-18 29.28 13.88 15.53 13.93 15.43 27.48 20.35 26.5 26.5 8.05 8.89 10.62 8.88 8.86 5.51 50 100 120 75 85 150 170 125 135

5SV-20 31.64 13.88 15.53 13.93 15.43 29.44 22.31 28.46 28.46 8.05 8.89 10.62 8.88 8.86 5.51 53 100 120 75 85 153 173 128 138

5SV-21 7.5

213TC 184TC

32.23 13.88 15.53 13.93 15.43 30.43 23.31 29.45 29.45 8.05 8.89 10.62 8.88 8.86 5.51 54 100 120 75 85 154 174 129 139

5SV-23 34.2 13.88 15.53 13.93 15.43 32.4 25.28 - 31.42 8.05 8.89 10.62 8.88 8.86 5.51 56 100 120 75 85 156 176 131 141

5SV-25 36.17 13.88 15.53 13.93 15.43 34.37 27.24 - 33.39 8.05 8.89 10.62 8.88 8.86 5.51 58 100 120 75 85 158 178 133 143

5SV-26 37.23 13.88 15.53 13.93 15.43 35.35 28.22 - 34.37 8.05 8.89 10.62 8.88 8.86 5.51 59 100 120 75 85 159 179 134 144

5SV-27 10 215TC 213TC 215TC 38.22 16.63 16.68 15.55 15.51 36.33 29.2 - 35.35 8.77 10.62 10.18 10.18 10.28 4.13 60 132 145 107 122 192 205 167 182

All dimensions are in inches (mm).

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29

5SV Curve 3500 RPM

13

12

10

9

8

7

6

5

4

3

2

21

14

15

20

17

11

23

25

26

27

TOTAL STAGES 5SV 60Hz3500 RPM

Q [m3/hr]

MINIMUM FLOW RATE: 7 GPM [1.6 m3/hr]

rickLine

rickText Box110 psi

17

TOP-FLO TF-C Series Centrifugal Capacity Curves

Based on water at 70F (22C)Model: C11460 Hz 3500 RPM

Size: 1-1/2 x 1-1/2 x 4

PROCESS EQUIPMENT COMPANYOffice: 0/"OXs"RADFORD0!Plant: 6ALLEY(UNT$RIVEs,EWIS2UN0!Phone: ssFAX

NOTES:

)MPELLERDIAMETERSAVAILABLEININCHINCREMENTS1 +GCM2 = (EADIN-ETERS83PECIlC'RAVITY

4

3 PSI = (EADIN&EET83PECIlC'RAVITY 2.3

(0X+W2 .03(2ISSHOWNFORMAXIMUMIMPELLERDIAMETER

CUBIC METERS PER HOUR

HE

AD

IN

FE

ET

HE

AD

IN

ME

TE

RS

3

4

US GALLONS PER MINUTE

CUBIC METERS PER HOUR

US GALLONS PER MINUTE

ME

TE

RS

FE

ET

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27

TOP-FLO TF-C Series

Close-Coupled Pump Dimensions

AND&RAME-OTORSTO&RAME-OTORS$$)-%.3)/.&!#%/&).,%44/#%.4%2//.$5)4/0%.).'

Pump Model Suction Discharge X* X** Y* Y** Z

4 4 4 4

Pump Dimensions (Easy-Clean totally-enclosed motor)

Pump

Model Frame A A1 B B1 C* C1* C** C1** D* D** HD AA AB

# 4#

# 4# 4# 4#

4# 4# 4# 4# 4#

4# 4# 4# 4# 4# 4#

Pump and Motor Dimensions with Easy-Clean Totally Enclosed Motors

TF-C114

TF-C216

TF-C218

TF-C328

7ITHCLAMPCONNECTIONS

7ITHTHREADEDBEVELSEATCONNECTIONS

$IMENSIONSAREAPPROPRIATEANDFORGUIDANCEONLY/.APPLICATIONSWHEREEXACTDIMENSIONSAREREQUIREDREQUESTACERTIlEDPRINTFROM4OP,INE

./4%3$IMENSIONSFORSINGLEPHASEFRAMEMOTORSLONGER

4HESEDIMENSIONSAREFORPUMPSUSINGSTANDARD#&LANGE-OTORS4ERIESPUMPSWILLNOTACCEPT43#&RAME-OTORS

25

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7GOULDS PUMPSCommercial Water

Performance Curves 60 Hz, 3500 RPM Curvas de Funcionamiento 60 Hz, 3500 RPM

m3c hr

10

20

40

50

6

70

80

90

110

5

10

20

30

160140120100806040200

151050

U.S. GPM

100

20 25 30

30

25

15

3 HP2 HP

1 1c2 HP1 HP

3c4 HP

5'

7'

10'

15'

20'

50

5558 60 62

64

66

64

6260

58EFF %55

Model NPE / 2ST Size (Tamao) 11c4 x 11c2-6RPM 3500 Curve (Curva) CN0235R01

B 51c16" DIA.

D 45c8"

E 41c4"

F 37c8"

METERSMETROS

FEETPIES

TOTA

L D

YNA

MIC

HEA

D (C

ARG

A D

INA

MIC

A T

OTA

L) H

CAPACITY (CAPACIDAD) Q

NPSHR FEET (PIES) NOTE: Not recommended for operation beyondprinted H-Q curve.NOTA: No se recomienda para funcionamientosuperior al impreso en la curva H-Q.

Impeller Selections for Exp. Proof MotorsSelecciones del Impulsor para Motores Exp. Proof

m3c hr

10

20

40

50

60

70

80

90

110

5

10

20

30

160140120100806040200

151050

U.S. GPM

100

20 25 30 35

30

25

15

40

Model NPE / 2ST Size (Tamao) 11c4 x 11c2-6RPM 3500 Curve (Curva) CN0235R02

120

130

35

METERSMETROS

FEETPIES

TOTA

L D

YNA

MIC

HEA

D (C

ARG

A D

INA

MIC

A T

OTA

L) H

CAPACITY (CAPACIDAD) Q

NPSHR FEET (PIES) NOTE: Not recommended for operation beyond printed H-Q curve.NOTA: No se recomienda para funcionamiento superior alimpreso en la curva H-Q.

Impeller Selections for ODP & TEFC MotorsSelecciones del Impulsor paraMotores ODP & TEFC

C 47c8"D 45c8"

E 41c4"

F 37c8"

A 51c4"B 51c16"

H 51c2"

G 515c16" DIA. 58

60

66

64

62 58

55

5055

EFF %

10'

15'

7'5'

20'

3c4 HP

1 1c2 HP1 HP2 HP

5 HP

3 HP

Ordering Standard Code, HP Rating, Imp. Cdigo Estndar HP Dia. de Pedido Potencia

F 1 378

E 1 4

D 2 458

B 3 5116

Ordering Standard Code, HP Rating, Imp. Cdigo Estndar HP Dia. de Pedido Potencia

F 378

E 1 4

D 1 458

C 2 478

B 3 5116

A 3 5

H 5 5

G 5 51516

NOTE: Although not recommended, the pump may pass a 316 sphere.

NOTA: Si bien no se recomienda, la bomba puede pasar una esfera de 316.

NOTE: Although not recommended, the pump may pass a 316 sphere.

NOTA: Si bien no se recomienda, la bomba puede pasar una esfera de 316.

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12


NPE Close Coupled Dimensions, Weights and Specifications NPE Acople Cerrado Dimensiones, Pesos y Especificaciones

Clockwise Rotation Viewed from Drive EndRotacin en Direccin de las Agujas del Reloj Visto desde el Extremo del Motor

Specifications Especificaciones

Capacities to: 85 GPM (322L/min) at 1750 RPM 170 GPM (643L/min) at 3500 RPM

Heads to: 39 feet (12 m) at 1750 RPM 150 feet (46 m) at 3500 RPM

Working pressures to: 125 PSIG (9 bars)

Maximum temperatures to: 250 F (121 C)

Direction of rotation: Clockwise when viewed from motor end.

Capacidades:85 GPM (322L/min) a 1750 RPM 170 GPM (643L/min) a 3500 RPM

Cargas: 39 pies (12 m) a 1750 RPM 150 pies (46 m) a 3500 RPM

Presin de trabajo:125 PSIG (9 baras)

Temperatura mxima:250 F (121 C)

Direccin de rotacin: En direccin de las agujas del reloj visto desde el extremo final del motor.

Motor specifications: NEMA 56J frame, 1750 RPM,

HP. 3500 RPM through 5 HP. Open drip-proof, totally enclosed fan-cooled or explosion proof enclosures. Stainless steel shaft with ball bearings.

Single phase: Voltage 115/230 ODP and TEFC. (3 and 5 HP model 230 V only) Built-in overload with auto-reset provided.

Three phase: Voltage 208-230/460 ODP, TEFC and EX PROOF.

NOTE: For three phase motors, overload protection must be provided in starter unit. Starter and heaters must be ordered separately.

Motores: Armazn 56J NEMA, 1750 RPM

HP. 3500 RPM a 5 HP. Cubiertas abiertas resguardadas, totalmente encerradas enfriadas por ventilador o a prueba de ex-plosiones. Eje de acero inoxidable con balineras de bolas.

Monofsicos: Voltaje 115/230 ODP y TEFC. (modelo 3 y 5 HP 230 voltios solamente) Se proporciona proteccin trmica contra sobrecarga construida con reseteo automtico.

Trifsicos: Voltaje 208-230/460 ODP, TEFC y EX PROOF.

NOTA: Para motores trifsicos se debe de proporcionar la proteccin trmica contra sobrecarga en la unidad de arranque. El arrancador y los calen-tadores se deben pedir por separado.

X

41c4

41c4

215c16

FILL AND VENT

CARGA Y VLVULA

DRAIN PLUG 3c8ENCHUFE DE DRENAJE 3c8

67c8

DISCHARGE

DESCARGA

3c16

Y W C MAX.

215c163c4

(4) 13c32 DIA. MOUNTING HOLES(4) 13c32 DIA. AGUJEROS DE MONTAJE

L 5

61c2

30oTYP.

65c16 MAX.

23c4

SUCTION

SUCCIN

4311/16

MAX.

1 PHASE UNITS ONLY

UNIDADES MONOFSICASSOLAMENTE

WY

L 5 131c3281c4

311c16MAX.4

61c2 MAX.

23c4

C MAX.

1 PHASE ONLY

MONOFSICASOLAMENTE

41 c4

X

81c8

DRAIN

DRENAJE

SUCTION

SUCCIN

FILL AND VENT

CARGA Y VALVULA

DISCHARGE

DESCARGA

13c32 DIA. HOLE4-MOUNTING HOLES13c32 DIA. 4-AGUJEROSDE MONTAJE

215c16

30TYP

215c16

41 c4

MOTOR CRADLE

HORQUILLA DEL MOTOR

ODP and TEFC , and 1 HP (standard), ODP y TEFC , y 1 HP (estndar)

ODP and TEFC 1, 2 and 3 HP (standard), ODP y TEFC 1, 2 y 3 HP (estndar)

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13


16 21 47 19 18 27 91516

19 24 41 21 21 30 10

1 22 26 49 23 21 30 11

1 28 35 56 27 27 37 11516

2 33 39 60 32 33 44 12116

3 40 43 41 37 12716

5 42 42 45 14

NPE Close Coupled with Footed Motor, Explosion-proof and 5 HP Motors

NPE Acople Cerrado con Motor con Patas, Motores a Prueba de Explosin Y 5 HP

Pump, Suction, Discharge, Bomba Succin Descarga

1ST 1 1 3 3 516 438 2 4916 7516

2ST 1 1 5 3 4 218 518 778

3ST 2 1 1 5 3 458 218 518 778

HP W X Y L M

Dimensions Determined by Pump, Dimensiones Determinadas por la Bomba

Pesos y Dimensiones Disponibles del MotorAvailable Motor Weights and Dimensions,

HPC Max. Length,

(Longitud)

Dimensions in inches, weights in pounds.Dimensiones en pulgadas, pesos en libras.

81/2

41/4 W

DISCHARGE

DESCARGA

61/2 DIA.

1/3

3

33/4

M

DRAIN PLUG 3/8

ENCHUFE DE DRENAJE 3/8

FILL AND VENT

CARGA Y VLVULA

SUCTION

SUCCIN

C. MAX.

41/4

X

Y

61/2

47/8

7/8

31/2

NOTES:1. Pump will be shipped with top

vertical discharge position as standard. For other orientations, remove casing bolts, rotate discharge to desired position, replace and tighten 6mm bolts to 5 6 lbs.-ft.

2. Motor dimensions may vary with motor manufacturers.

3. Dimensions in inches, weights in pounds.

4. For explosion proof motor dimensions consult factory for information.

5. Not to be used for construction purposes unless certified.

NOTAS:

1. Las bombas se transportarn con la descarga vertical superior como estndar. Para otras orien-taciones, retirar los tornillos de la carcasa, rotar la descarga a la posicin deseada, y reemplazar y apretar los tornillos de 6mm a 5 6 libras-pies.

2. Las dimensiones del motor puede que varen con los fabricantes.

3. Dimensiones en pulgadas, pesos en libras.

4. Para las dimensiones de los motores a prueba de explosin consultar con la fbrica para informacin.

5. No usar para propsitos de construccin sin certificar.

ODP TEFCODP TEFC EXP EXP

1 Phase, Monofsicos 3 Phase, Trifsicos

Motor Weights, Pesos del Motor

All Explosion Proof Motors and 5 HP ODP and TEFC

Todos los motores son a prueba de explosiones, 5 HP, ODP

(abiertos resguardados) y TEFC (totalmente encerrados con

enfriamiento forzado)

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PNEUMATICS M


I/O LIST N



FLASH PASTUERIZER 11FP353 I/O LISTING SHORTS BREWING CO. 6/09/11

INPUTS OUTPUTS I:0.0/0 FLOW METER (PULSE) O:0.0/0 (P1) MBP STARTER I:0.0/1 SLT HL PROBE O:0.0/1 (P2) BBP VFD STARTER I:0.0/2 SLT LL PROBE O:0.0/2 (P3) HWR STARTER I:0.0/3 AV1 CLOSED O:0.0/3 SPARE I:0.0/4 AV2 CLOSED O:0.0/4 CIP FLOW VALVES I:0.0/5 AV3 CLOSED (JB1) O:0.0/5 AV1 OPEN I:0.0/6 AV4 CLOSED (JB1) O:0.0/6 AV2 OPEN I:0.0/7 AV5 CLOSED (JB1) O:0.0/7 AV3 OPEN I:0.0/8 SEQUENCE STOP O:0.0/8 AV4 OPEN I:0.0/9 MBP RUNNING O:0.0/9 AV5 OPEN I:0.0/10 BBP RUNNING O:0.0/10 AV6 OPEN I:0.0/11 HWR RUNNING O:0.0/11 SEQUENCE STOP LAMP I:0.0/12 BBP CONTROL MK1 (REMOTE) O:1.0/0 AUDIBLE ALARM I:0.0/13 BBP CONTROL MK2 (REMOTE) O:1.0/1 RED STACK LAMP - UHL SPT I:0.0/14 FEED PROTECT PROBE (OPT) O:1.0/2 CLEAR STACK LAMP - HL SPT I:0.0/15 SPARE O:1.0/3 AMBER STACK LAMP - ML SPT I:0.0/16 SPARE O:1.0/4 GREEN STACK LAMP - LL SPT I:0.0/17 SPARE O:1.0/5 BLUE STACK LAMP - ULL SPT I:0.0/18 SPARE I:0.0/19 SPARE NOTE: FOR CIP MODE, BLINK BLUE STACK LAMP, O:1.0/1

ANALOG INPUTS ANALOG OUTPUTS I:0.0/V0+ SPT DIFF. PRES. TRANS. (DP1) I:0.0/V1+ BEER PRES. TRANSDUCER O:0.0/OV0 CHART REC. HOLD TUBE TEMP. O:0.0/OV1 CHART REC. PROD. OUT TEMP.

RTD INPUTS O:2.0/0 STEAM I/P CONVERTER O:2.0/1 GYLCOL I/P CONVERTER I:3.0/0 RTD 1 HOLDING TUBE TEMP. O:2.0/2 CHART REC. CIP RETURN TEMP I:3.0/1 RTD 2 PRODUCT OUT TEMP. O:2.0/3 VFD SPEED CONTROL I:3.0/2 RTD 3 CIP RETURN TEMP. (OPT)




6 CORE COLOR CODE - JUNCTION BOX (JB1)

ADDRESS INPUTS COLOR I:0.0/5 AV3 CLOSED BLUE I:0.0/6 AV4 CLOSED GREEN I:0.0/7 AV5 CLOSED WHITE

24VC 24VDC CONTROL RED

0VC 0VDC CONTROL BLACK




12 CORE COLOR CODE - JUNCTION BOX (REMOTE)

ADDRESS INPUTS COLOR (CABLE) I:0.0/12 BBP CONTROL MK1 ORG (REMOTE INPUTS) I:0.0/13 BBP CONTROL MK2 YEL (REMOTE INPUTS)

24VDC CONTROL + VIOLET (REMOTE INPUTS)

OUTPUTS

O:1.0/1 RED STATUS LAMP RED (REMOTE OUTPUTS) O:1.0/2 CLEAR STATUS LAMP WHITE (REMOTE OUTPUTS) O:1.0/3 AMBER STATUS LAMP BROWN (REMOTE OUTPUTS) O:1.0/4 GREEN STATUS LAMP GREEN (REMOTE OUTPUTS) O:1.0/5 BLUE STATUS LAMP BLUE (REMOTE OUTPUTS)

0VS COM BLACK (REMOTE OUTPUTS)



FLASH PASTUERIZER 11FP353 SHORTS BREWING CO. 6/09/11

TWISTED PAIR 4 COND. - JUNCTION BOX (REMOTE)

ADDRESS INPUTS COLOR (CABLE) I:0.0/V1+ SPT DIFF. PRES. TRANS PAIR TWO - RED

24VDC ANALOG + PAIR ONE - RED 0VDC ANALOG - PAIR ONE - BLACK


OXINE O

Manual Oxine Dilution & Use

Useful figures to have available if you are diluting Oxine manually without a titration kit. These figures are applicable with Oxine that has been activated within 48 hours of dilution with a food grade acid at 2.5 to 3 pH . For keg sanitizing and use with the Super King, Mini King or Squire series machines: It is recommended that you start by using approximately 100 ppm of activated Oxine for keg sanitizing until you can determine through your own QC procedures whether you need to increase or decrease the amount based upon microbial results obtained. Experience indicates that normal usage will be in the range of 20 to 100 ppm. 1. Take a one gallon container with a screw lid and drill a hole in the cap to suit the dosing unit siphon tube. 2. Take 0.6 liter (20 ounces) of Oxine, add food grade acid to lower the pH to approximately 2.5 to 3.0 pH to activate the Oxine and stir. This will give you approximately 20,000 ppm of activated Oxine. CAUTION Do so in a well ventilated area and do NOT breathe the fumes given off during activation. See the MSDS in this section for more details. 3. When activated (after 5 to 10 minutes) add 3 liters (101 ounces) of water to the activated Oxine (5:1 ratio). This will give you approximately 4,000 ppm of activated Oxine. Stir and replace cap with siphon tube into Oxine. 4. Using the chart supplied with the Oxine doser venturi kit select the colored venturi that will then give you a 40:1 reduction ratio. This will give you approximately 100 ppm of activated Oxine being supplied as your rinse and sanitizing water to the keg for pre and post rinse. 5. This can be verified with the Oxine test kit or Oxystix attainable from IDD Process & Packaging, Inc.

Other ratios of Oxine for general sanitizing purposes One unit of manually activated Oxine at 20,000ppm and you: Add 1 unit of water, the concentration reduces to 10000ppm Ratio of water to Oxine 1:1. Add a further 2 units of water, the concentration reduces to 5000ppm Ratio of water to Oxine 3:1. Add a further 4 units of water, the concentration reduces to 2500ppm Ratio of water to Oxine7:1. Add a further 8 units of water, of the concentration reduces to 1250ppm Ratio of water to Oxine 15:1. Add a further 16 units of water, the concentration reduces to 625ppm Ratio of water to Oxine 31:1. Add a further 32 units of water, the concentration reduces to 312.5ppm Ratio of water to Oxine 63:1. Add a further 64 units of water, the concentration reduces to 156.5ppm Ratio of water to Oxine 127:1. Add a further 128 units of water, the concentration reduces to 78ppm Ratio of water to Oxine 255:1. Add a further 256 units of water, the concentration reduces to 39ppm Ratio of water to Oxine 511:1. Add a further 512 units of water, the concentration reduces to 19.5ppm Ratio of water to Oxine 1023:1. Add a further 1024 units of water, the concentration reduces to 9.5ppm Ratio of water to Oxine 2047:1. Add a further 2048 units of water, the concentration reduces to 5ppm Ratio of water to Oxine 4095:1. Add a further 4096 units of water, the concentration reduces to 2.5ppm Ratio of water to Oxine 8191:1. Add a further 8192 units of water, the concentration reduces to 1.25ppm Ratio of water to Oxine 16382:1.

OXINE & PUROGENE SANITIZER


The following information is offered as suggested uses of Oxine and Purogene and is not intended to be definitive or accurate for all applications. IDD Process & Packaging, Inc. do not accept any liability for the use or application of Oxine or Purogene.

OXINE AND PUROGENE...THE SANITIZERS FOR ALL REASONS. For years it has

been known that chlorine dioxide gas is a powerful anti-microbial agent. However, this gas is toxic and unstable in an aqueous solution. Modern technology has overcome these problems with Oxine and Purogene. Today, stabilized chlorine dioxide (ClO2) is available in a concentrated stable form with very low toxicity. As a powerful oxidant, stabilized ClO2 is virtually unaffected by organic load and hard water. These technical advances have resulted in the FDA, EPA and USDA approving stabilized ClO2 as an acceptable sterilant for numerous applications within the brewery, dairy and food processing plants. Properties which make stabilized ClO2 most attractive to the brewer, maltster and other beverage plant operators are:

LOW ODOR - Unlike typical sanitizers such a hypochlorites, quaternary ammonium, or

even peroxy-acetic acid, stabilized ClO2 has an almost undetectable odor while surpassing the bacteriocidal efficacy of these other compounds. Hypochlorites can form chlorophenols (a medicinal flavor compound) when combined with organic material in beer: Quaternary ammonia compounds have well known negative effects on flavor; the end product of the reduction of peroxy-acetic acid is acetic acid, with its typically "vinegar-like" character. Even small amounts remaining in a tank and having the opportunity of coming in contact with beer, can have a deleterious effect on beer flavor.

LOW CORROSIVITY - Stabilized ClO2 is not harmful to vessels or piping systems

when used at the recommended dosages. Typically, brewers like the effectiveness of hypochlorites but a major drawback is hypochlorites role in causing stress corrosion fatigue in stainless steel, particularly at weld joints. Stabilized ClO2 while actually being 4 to 7 times more effective as a sanitizer than hypochlorite, does not enhance or contribute to stress corrosion fatigue in the metal. Stabilized ClO2 is only slightly more corrosive than tap water at and much of this is due to the acid used in the activation of the product. When it is used as a final rinse in vessels, or piping systems, it is perfectly safe to leave a 10 ppm solution un-rinsed in a tank, pipe network or piece of process equipment, (i.e. bottle fillers, keg racking machines, sheet or pressure leaf filters, etc.).

EASE OF HANDLING - While idophors, peroxy-acetic acid and hypochlorites are

popular sanitizers for tanks, fillers and other equipment, they have some handling drawbacks. Iodophors are really only effective at low pH, thus they are typically carried as a concentrate in a solution of phosphoric or nitric acid. This makes them hazardous to handle. Iodophors also have a tendency to stain equipment (and people). Pereoxy-



acetic acid is actually quite volatile at moderately elevated temperatures (120_F/50_C) and can cause spontaneous explosions. It is also corrosive in its concentrated form. Hypochlorites as chlorine gas have a short-term exposure limit slightly higher than that of stabilized ClO2 (1.0 ppm versus 0.3 ppm respectively). However, since stabilized ClO2 is 4 to 7 times more effective than hypochlorites at normal use levels, it is less hazardous.

NO ENVIRONMENTAL IMPACT - Stabilized ClO2 does not form the highly

carcinogenic trihalomethanes as do hypochlorites in the presence of organic materials. Oxine is environmentally and user friendly and has been accepted by the EPA has having no environmental impact upon disposal. It is not corrosive nor is it volatile in its concentrated (2%) form.

EFFICACY - Stabilized ClO2 does not act by chlorination but by oxidation and has

proven effective against all common brewery, winery and beverage plant micro- organisms. It is an effective bacteriostat at use rates as low as 5 to 20 ppm against such common pests as Lactobacillus and Pediococcus sp. and at 50 ppm against Wild Yeasts and Mold strains.

As with all gaseous products such as stabilized ClO2, Oxine can be monitored by

using a standard gas monitoring system such as those supplied by LAB SAFETY SUPPLIES COMPANY. Toll free telephone number 800-356-0722. It is necessary to take extra care with good ventilation during the "activation" process of Oxine. If it is considered necessary to monitor gas levels at this time for your safety records, we recommend that the chlorine "low range" (0.05 to 16ppm) tube be used to monitor gas levels. These tubes readily detect and measure all types of inorganic chlorine.

MALTHOUSE: Stabilized ClO2 is an effective wash down sanitizer for walls and floors, germination

areas and steep tanks. At 100 to 500 ppm it will kill and bleach out mold and mildew common to these high-humidity areas. Stabilized ClO2 is successfully used in barley steep waters to inhibit microbial growth of all types. Typically at 10 to 50 ppm depending on the microbial load, one can assure a safe re-cyling of the steep water into subsequent batches. Stabilized ClO2's strong oxidizing capability actually reduces B.O.D. loads for disposal.

BREWHOUSE: Safe for all vessels and piping systems, whether copper or stainless steel, stabilized

ClO2 can ensure a microbially free environment in coppers/kettles, mash filters or lauter tuns, swirl tanks, settlers and wort cooling systems when used at 50 to 100 ppm. The related piping systems for wort transfer to fermentation areas can be sanitized at 100 ppm. A 50 ppm solution is also safe to leave in the pipelines during periods of non- use, to keep them sanitized.



FERMENTATION/STORAGE AREAS: A 50 ppm solution is adequate to sanitize tank walls and related piping systems.

Since low levels of contact with finished product do not effect final beer flavor, one can safely use stabilized ClO2 in a final rinse and be able to obtain some residual bacteriostatic value. It is recommended that boots, gloves, yeast-handling tools and the like be sanitized at 100 ppm. Stabilized ClO2 at 100 ppm is ideal for foot baths at or near tank entry areas.

FILTRATION: Stabilized ClO2 is particularly useful for stabilizing and sanitizing filter systems. It can

be used to shock sanitize activated carbon and sand/gravel filters in the water treatment facility. Typically, a 50 to 100 ppm solution is run slowly through these type filters. Stabilized ClO2 will not be absorbed significantly by the active carbon. Once the bed is sanitized it is then possible to dose Oxine into the water stream prior to the filter bed at a concentration of 1 to 5 ppm in order to prevent future contamination.

Plate-and-frame filters can be sanitized with a 10 to 50 ppm solution without the

typical water flush/rinse required by acid-sanitizers and the like. A standing solution of up to 10 ppm can be left in a filter during periods of non-use with no harm to the filter frame or the sheets.

It is recommended that this procedure be carried out after any normal beer filter use to

inhibit the growth of yeasts and bacteria, since residual beer on the sheets makes for an ideal growth media. A solution of the same strength sprayed over the outer exposed edges of the filter sheets will prevent mold growth when standing.

PACKAGING: Stabilized ClO2 provides a safe sanitization and soaking solution for keg washer

rackers, bottle and can fillers. Sanitize at 50 ppm and soak or stand filler bowls in cold water at 10 ppm.

Aseptic keg, bottle and can rinsing immediately prior to filling with beer is enhanced

when 20 to 50 ppm of stabilized ClO2 is used as a final cold rinse.

The use of stabilized ClO2 as an aseptic "fog" spray around aseptic bottle and can fillers is highly effective as a sanitizer and microbial preventative at 10 to 20 ppm.

The non-corrosive nature of stabilized ClO2 makes it an ideal growth inhibitor in tunnel

pasteurizers. Stabilized ClO2 is most effective in the moderate temperature zones (warm-up and cool-down fresh water zones) of the pasteurizer. A 20 to 30 ppm solution is normally adequate and quite safe to the equipment.



TANK-TRUCK WASHING: As in the typical use for tank washing and sanitizing, stabilized ClO2 can be used for

the sanitization and cleanup of bulk tankers and their related piping and hoses. Wash down tank internals, pumps and hoses at 100 ppm, externals at 250 to 500 ppm. This will prevent transfer of micro-organisms to or from the connecting systems.

MOLD AND MILDEW CLEANUP AND CONTROL: Clean off walls and floors as well as air handling units and machinery using a 200 to

500 ppm solution of stabilized ClO2. This effectively kills mold and mildew spores while still retaining some bleaching ability to remove tough black stains. This is good procedure prior to painting, or prior to the application of a mold and slime growth inhibitor such as Alltech's Mold-Zap.

PROCESS WATER TREATMENT: The FDA has approved stabilized ClO2 for process water sanitization at between 100

to 200 ppm available ClO2. Potable water treatment is approved for human consumption at 4 ppm available ClO2.

ACTIVE CARBON BED (ACB): Infected ACB's can be back flushed and soaked in a 100 ppm solution of ClO2 for 15

to 60 minutes, after which time a forward flush-out of 15 to 30 minutes with the process water can take place. It is then advisable to inject 1 to 3 ppm of activated ClO2 into the process water stream thereafter prior to the ACB to prevent future infections.

GLASS WASHING/RINSING: Even at the final stage of the brewer's trade, where bars and pubs have a need for an

effective and safe drinking-glass sanitizer, stabilized ClO2 can fill the need. Since stabilized ClO2 can be safely consumed at 4 ppm, it makes an ideal glass rinse. Unlike typical quaternary ammonium rinses, it will not have any deleterious effect on beer flavor, nor on beer foam quality. Use at 20 to 50 ppm in final rinse water.

WASHING OF YEAST SLURRY WITH STABILIZED ClO2 (OXINE): Stabilized ClO2 (Oxine) will effectively kill unwanted bacteria in yeast at 20 to 40 ppm,

while leaving the culture yeast unharmed. Because of stabilized ClO2's unique action, it does not have the drawbacks of phosphoric acid. It does not form chlorophenols (which contribute to a much feared medicinal character in beers) in the presence of organic materials.

METHOD: Normally, an initial washing at 20 to 40 ppm (20 ppm for homogenous yeast, 40 ppm

for "clumpy" or highly flocculant strains) is effective against most Lactobacilli and Pediococci species. This "wash" is done by adding stabilized ClO2 directly to yeast slurry on a volume/ppm basis. It does not need to be activated as the pH of the yeast slurry is low enough to convert to ClO2.



Stabilized ClO2 is supplied at a concentration of 20,000 ppm or 2% Chlorine Dioxide when activated. Therefore, on a volume basis, one could essentially make up with one gallon of stabilized ClO2 concentrate, one thousand gallons of solution at 20 ppm. By this method, we can also assume with one gallon of concentrate to make up one thousand gallons of yeast slurry at 20 ppm. It is impractical to measure the concentration of ClO2 in the presence of yeast, so the dilution must be made based on the strength of the concentrate (20,000 ppm).

Yeast slurry should be thin enough to allow for homogeneous mixing, usually 20 to

40% solids. The killing action of stabilized ClO2 is very fast compared to the traditional phosphoric acid wash. Only 15 to 30 minutes need be allowed for effective bactericidal effect of stabilized ClO2, with no resultant stress on yeast cells.

DOSING RATE: NORMAL WASH: For regular washing of homogenous recycled brewers yeast, a 20

to 40 ppm wash for a minimum 30 minutes to 5 hours prior to pitching. Mix 1 to 2 ml of stabilized ClO2 concentrate with each liter of yeast slurry. Agitate thoroughly during the process.

ACTIVATION OF CONCENTRATE: Since the ClO2 is in a stabilized form in concentrate, it must be "activated" before

using. To activate Oxine add acid to lower the pH in a well ventilated area to below 5 pH. Activation can be verified by a corresponding color change of the concentrate from clear to yellow/green. Any number of acids will activate the stabilized ClO2, however, food grade Citric or Phosphoric acid is recommended for this application.

Normally it requires up to 200 grams of Citric Acid to activate one gallon of stabilized

ClO2 concentrate (up to 50 grams per liter of stabilized ClO2 concentrate).

Following are the details for replacement chemicals for your Oxine Test Kits.

10% Potassium Iodide - 100 g diluted to 1,000 ml with distilled water.

0.2N Hydrochloric Acid - Add 16.6 ml Concentrated HCL (39%) to 800 ml water. Bring to 1,000 ml with water.

0.00564N PAO (Phenylarsine Oxide).

Oxine is available from IDD in 1, 5, 30, 55 gallon and tote containers. Test kits and

replacement materials can also be purchased from IDD.



STORAGE: Concentrated ClO2 can be stored in a dry area away from acids for up to 3 years

under standard conditions.

Activated ClO2 has a half-life of approximately 48 hours under standard conditions.

Activated ClO2 can be added to cold water at 4,000 ppm. Under such conditions a half-life of up to 2 weeks is possible under standard conditions.

AUTOMATIC ACTIVATION SYSTEMS:

A series of low cost, hands free, automated activation systems are available to provide a continuous volume of activated ClO2 into a storage reservoir as needed. These systems eliminate the need for manual mixing, measuring and dispensing.

INTERNATIONAL, INC.

MATERIAL SAFETY DATA SHEETI

SECTION 1: CHEMICAL PRODUCT AND COMPANY IDENTIFICATION

PRODUCT NAMEOxine

CHEMICAL FAMILYMixture of Oxychlorine Compounds

MANUFACTURERBio-Cide International, Inc., 2845 Broce Drive, Norman, OK 73072 U.S.A. (800.323.1398)

EPA REGISTRATION NUMBER:9804-1

EFFECTIVE DATE:June 2004

SUPERSEDES:April 2002

SECTION 2: COMPOSITIONIINFORMATION ON INGREDIENTS

Chemical NameSodium Chlorite

C.A.S. No.7758-19-2

% by Wt.3.35%

SECTION 3: HAZARDS IDENTIFICATION

EMERGENCY OVERVIEWClear liquid with very faint chlorinous odorMay cause skin reaction. May cause eye irritation.

POTENTIAL HEALTH EFFECTS

INHALATION: Prolonged inhalation of fog or mist may be irritating to nose and throat.SKIN: Based on rabbit studies, product is listed as "practically not an irritant".

Prolonged exposure may produce localized irritation, contact dermatitis, milderythema and edema.

EYE: Based on rabbit studies, product has been given an EPA Category III rating as amild irritant. Exposure can produce slight irritation of conjunctiva, cornea andeyelid.

INGESTION: Ingestion may produce gastric discomfort, nausea, vomiting and diarrhea. Intakeof large quantities may produce methemoglobinemia.

SYSTEMS OF OVER EXPOSURESkin and eye irritation. Exposures to chlorine dioxide from activation can produce coughing.

MEDICAL CONDITIONS AGGRAVATED BY EXPOSURESkin disorders, such as dermal allergies and dermatitis. Exposure to chlorine dioxide producedby activation can aggravate pulmonary disorders, such as emphysema.

- 1 -

CHRONIC EXPOSURE EFFECTSMay cause localized irritation to areas exposed to product.

,

SECTION 4: FIRST AID MEASURES

The following procedures are recommended as emergency first aid only. They are not intended toreplace or supplant the treatment advice of a physician or other authorized health care specialist.

Inhalation: Move person to fresh air. If person is not breathing, call 911 or an ambulance, and thengive artificial respiration, preferably mouth-to-mouth if possible. Call a poison control center or doctor forfurther treatment advice.

Skin Contact: Take off contaminated clothing. Rinse skin immediately with plenty of water for 15-20minutes. Call a poison control center or doctor for further treatment advice.

Eye Contact: Hold eye open and rinse slowly and gently with water for 15-20 minutes. Removecontact lenses, if present, after the first 5 minutes, then continue rinsing eye. Call a poison control centeror doctor for further treatment advice.

If Swallowed: Call a poison control center or doctor immediately for treatment advice. Have personsip a glass of water if able to swallow. Do not induce vomiting unless told to do so by a poison controlcenter of doctor. Do not give anything by mouth to an unconscious person.

NOTES TO PHYSICIAN

Chlorine dioxide vapors are emitted when this product contacts acids or chlorine. If these vaporsare inhaled, monitor patient closely for delayed development of pulmonary edema which mayoccur up to 48-72 hours post inhalation.

SECTION 5: FIRE FIGHTING MEASURES

FLAMMABLE PROPERTIESAutoignition temperatureFlash PointFlammable Limits - LELFlammable Limits - UEL

Not ApplicableNot ApplicableNot ApplicableNot Applicable

EXTINGUISHING MEDIAWater unless contraindicated by other materials involved in the fire.

FIRE-FIGHTING EQUIPMENT

Standard protective gear with self-contained breathing apparatus.

SPECIAL FIRE-FIGHTING PROCEDURESDo not allow product to evaporate to dryness. If chlorine dioxide gas is produced, vent toatmosphere. Open or vent any large containers.

UNUSUAL FIRE OR EXPLOSIVE HAZARDS

The sodium chlorite in dried Oxine~ is a strong oxidizer, which supports combustion. Chlorinedioxide, which may evolve from Oxine'" solutions, is explosive in the gaseous phase atconcentrations greater than 10% by volume. Do not allow chlorine dioxide gas to accumulatewithin a confined space.

Note: See STABILITY AND REACTIVITY (SECTION 10) for hazardous combustion andthermal decomposition information.

-2-

SECTION 6: ACCIDENTAL RELEASE MEASURES

ENVIRONMENTAL NOTIFICATIONAll spills and leaks involving more than 10 gallons should be reported to the nearest regional EPAoffice or designated state emergency response office with 24 hours. Spills from ocean vessels orwhich may contaminate U.S. costal waterways should be reported to the nearest Coast Guardoffice within 24 hours.

SPILL OR LEAK PROCEDURESmall spills, involving less than 10 gallons, may be flushed to a designated and permitted sewersystem with the amount of water that is about 10 times the amount of the spill.

Large spills, involving more than 10 gallons, should be contained and neutralized using anyoneof the three neutralizers: i) sodium sulfite, ii) sodium bisulfite, or iii) sodium thiosulfate. Theneutralization reaction can be extremely exothermic, and therefore, care should be taken to addthe neutralizer in small increments. Sodium sulfite is the most preferred (least exothermic)neutralizer that can be used in the ratio of 1 Ib per gallon of spilled material. Sodium thiosulfatecan be used in the ratio of 2 Ibs of anhydrous salt or 3 Ibs of pentahydrate salt per estimatedgallon of the spilled material. The neutralized solution can then be flushed to a designated andpermitted sewer system with double the amount of water. The product that is not neutralized maybe disposed of as chemical waste in the manner indicated below. The vicinity of the spill shouldbe thoroughly flushed with water after clean-up. At no time should the spilled material be allowedto dry to a crystalline salt. Do not discharge this product to storm drains or to any surface orgroundwater source unless specifically allowed under a valid NPDES permit.

If the neutralizer is not available, volumes larger than 10 gallons should be carefully transferredinto a container and taken to an authorized chemical disposal site (Class I or landfill) inaccordance with all federal, state, and local regulations. Consult with selected facility regardingthe need for prior neutralization of waste.

SECTION 7: HANDLING AND STORAGE

HANDLINGUse product only as directed by the label. Avoid contact with skin and eyes; avoid breathing anyvapors or fumes resulting from product activation. Wash thoroughly after handling. Thoroughly rinseall protective gear and handling equipment, such as transfer pumps and lines, with water prior toreuse or storage. Keep away from children, animals, and unauthorized personnel.

PRODUCT STORAGEStore in a cool, dry, well-ventilated location away from acids, chlorine and chlorine compounds,hypochlorites (bleach), organic solvents, sulfur and sulfite compounds, phosphorus,combustiblelflammable materials, and direct sunlight. Keep containers tightly closed when not inuse and open carefully to prevent spillage. Storage on wooden floors and pallets is notrecommended. Do not contaminate water, food or feed by storage or disposal.

SECTION 8: EXPOSURE CONTROLS/PERSONAL PROTECTION

ENGINEERING CONTROLSVENTILATION

Open air or good room ventilation is normally adequate for safe use of this product. Avoidbreathing any vapors or fumes resulting from acid activation.

-3 -

PERSONAL PROTECTIVE EQUIPMENT (PPE)

Eye/Face Protection

Good manufacturing practice recommends use of chemical safety goggles for all applicationsinvolving chemical handling.

Skin Protection

Good manufacturing practice recommends that, at a rmrumurn, rubber, neoprene, or otherchemically impervious gloves be worn for all applications involving chemical handling.

Respiratory Protection

In accordance with OSHA regulations (29 CFR 1910.134 and 29 CFR 1910.1000), fogging orspraying applications may require worker respiratory protection, such as: (1) NIOSH/MSHAapproved air-purifying respirators, or (2) NIOSH/MSHA approved canister/cartridge facialrespirators rated for chlorine/acid vapors or specified for chlorine dioxide.

General

Product should be stored and applied in close proximity to a safety shower, chemical eyewashstation or other fresh water source.

SECTION 9: PHYSICAL AND CHEMICAL PROPERTIES

Odor, Color, GradeGeneral Physical FormVolatile Organic CompoundsFlash PointEvaporation RateSolubility in WaterBoiling PointVapor DensityVapor PressureSpecific GravitypHMelting point:

Clear liquid with very faint chlorinous odorLiquid

SECTION 11: TOXICOLOGICAL INFORMATION

ANIMAL TOXICOLOGYInhalation LC50:

Dermal LD50:Oral LD50:

CARCINOGENICITYActive ingredients are not listed by ROTECS, OSHA, IARC, NTP or EPA. No evidence to dateimplicating product as a carcinogen or tumor promoter.

>5.61 mg/I>2,020 mg/kg (rabbit)4,360 mg/kg (rat)

MUTAGENICITYThough product active ingredient is a chemical oxidant, no evidence to date for mutagenicity fromwhole animal or in vitro studies.

REPRODUCTIVE/DEVELOPMENTAL TOXICITYNo known effects to date.

SECTION 12: ECOLOGICAL INFORMATION

ECOTOXICOLOGICAL INFORMATIONThis product is toxic to fish and aquatic organisms. Do not discharge effluent containing thisproduct into lakes, streams, ponds, estuaries, oceans or other waters unless in accordance withthe requirements of a National Pollutant Discharge Elimination System (NPDES) permit and thepermitting authority has been notified in writing prior to discharge. Do not discharge effluentcontaining this product to sewer systems without previously notifying the sewage treatment plantauthority. For guidance, contact your State Water Board or Regional office of the EPA.

SECTION 13: DISPOSAL CONSIDERATIONS

CONTAINER DISPOSALTriple rinse. Then offer for recycling or reconditioning; or puncture and dispose of in a sanitarylandfill; or by incineration; or, if allowed by state and local authorities, by burning. If burned, stayout of smoke.

PESTICIDE DISPOSALWastes resulting from the use of this product may be disposed of on site or at an approved wastedisposal facility.

DISPOSAL PROCEDURESmall quantities, less than 10 gallons, may be flushed to an authorized and permitted sewer withcopious amounts of water. Larger volumes should be taken to an authorized chemical disposalsite (Class I or landfill) in accordance with all federal, state and local regulations. Consult withselected facility regarding the need for prior neutralization of waste.

SECTION 14: TRANSPORT INFORMATION

Not DOT Regulated

-5 -

SECTION 15: REGULATORY INFORMATIONUS FEDERAL REGULATIONS

TSCAAll product ingredients are in inventory

SARA TITLE 312/313Neither the product nor its constituent ingredients are listed under SARA reporting requirements.Chlorine dioxide produced from activation is listed under SARA 313.

RCRA

Not considered a hazardous waste either categorically or by chemical listing.

FIFRAOxine" is an EPA registered sanitizer (EPA No. 9804-1)

FEDERAL OSHA REGULATIONS

Neither product nor constituent ingredients is classified as an acute or chronic health hazard byOSHA. Chlorine dioxide produced by activation is regulated with an air exposure limit of 0.1 ppmTL V and 0.3 ppm STEL.

STATE LAWS

CALIFORNIA: Not regulated under the provisions of Proposition 65 (Safe Drinking Water andToxic Enforcement Act of 1986)

NEW JERSEY: Sodium Chlorite is listed under New Jersey's Chemical Inventory NotificationRequirement (NJAC 7:1Z). Estimated release notification, however, is not required.

NOTE: Regulatory requirements are subject to change and may vary from one location toanother. It is the user's responsibility to ensure compliance with all applicable federal, state andlocal regulations pertaining to the purchase, transport, storage, use and disposal of this product.

CHEMICAL INVENTORIESThis material contains one or more substances listed on the TSCA Inventory. Commercial use ofthis material is regulated by the EPA.

This MSDS has been prepared to meet the U.S. OSHA Hazard Communication Standard, 29 CFR 1910.1200

SECTION 16: OTHER INFORMATON

NFPA Hazard ClassificationHealth: 1 Flammability: 0 Reactivity: 1 Special Hazards: None

National Fire Protection Association (NFPA) hazard ratings are designed for use by emergency responsepersonnel to address the hazards that are presented by short-term, acute exposure to a material underconditions of fire, spill, or similar emergencies. Hazard rating primarily based on the inherent physicaland toxic properties of the material but also include the toxic properties of combustion or decompositionproducts that are known to be generated in significant quantities.

NOTICE: Manufacturer believes the information contained herein is accurate; however we make noguarantees with respect to such accuracy and assume no liability in connection with the use of theinformation contained herein by any party. Any party using this product should review all such laws, rulesor regulations prior to use.

Product may bleach clothing and fabric materials, such as draperies and carpets.

NO WARRANTY IS MADE, EXPRESS OR IMPLIED FOR A PARTICULAR PURPOSEOR OTHERWISE

-6-


PLANNED PREVENTATIVE MAINTENANCE P


DAILY:

1. Clean machine after use, with low pressure hose and warm soapy water. DO NOT HOSE DOWN THE ELECTRICAL PANELS

2. Check and monitor service pressures and temperatures prior to and during operation in line with operations manual recommendations.

3. Change caustic and/or acid detergents hourly and monitor pH levels as necessary. 4. Check the connection head spear adapters for damage. Change if necessary. Any damage may be

transferred to the keg valve seal. WEEKLY:

1. Check connection head seals and O rings for wear and damage. Replace if necessary. 2. Check for leaks on all service lines and unions. Replace seals and/or tighten as necessary. 3. Check for loose nuts and bolts. Tighten as necessary. 4. Check for loose wire terminations. Tighten as necessary.

MONTHLY:

1. Check dosing units for accuracy and operation in line with operations manual recommendations. Adjust if necessary.

2. Check fiber optic, I.R. and/or fiber optic probes for cleanliness and operation. Clean and/or replace if necessary.

3. Clean out all airline filters and drain out condensate. 4. Check all push button switches and indicator lamps for damage. Replace is necessary. 5. Clean out all steam strainers. 6. Check all spare parts inventory levels in line with operations manual. Order if necessary.

THREE MONTHLY:

1. Check pressure gauges for accuracy. Adjust and/or replace if necessary. 2. Check the transfer system alignment and keg placement over the connection heads. Adjust and/or

replace worn parts and lubricate if necessary. 3. Check all hoses for leaks and/or wear. Replace if necessary. 4. Check tri-clover seals for wear and/or damage. Replace if necessary. 5. Check pressure switch calibrations and adjust according to the manual if necessary. 6. Check all reject functions are operational on all process heads. 7. Check all electrical power connections and motor overload settings. Reset if necessary.

YEARLY:

1. Inspect all wearing strips. Replace if necessary. 2. Check process valve, seats, O rings and seals for wear. Replace if necessary. 3. Inspect pump seals for wear or damage. Replace if necessary. 4. Inspect all air cylinder seals for wear and/or damage. Replace if necessary. 5. Check nylon air lines for leaks and flexibility. Replace if necessary. 6. Check all solenoid valves for proper operation. Replace if necessary. 7. Replace seals on all process valves.

PLANNED PREVENTATIVE MAINTENANCE FOR SQUIRE, MINI KING, SUPER KING & EMPEROR SERIES KEGGING & FLASH PASTEURIZATION

SYSTEMS


DIMENSIONS R


RECOMMENDED SPARES PARTS S


SERVICES T

SERVICE REQUIREMENTS FOR 50 HL/HR FLASH PASTEURIZATION SYSTEM

NOTATION LOCATION SERVICE PRESSURE BAR

CONSUMPTION FLOW RATE TERMINATION COMMENTS

1 PASTEURIZER BEER 1 50 HL/HR 50 HL/HR 1.5 O/D TUBE 1 DEG C 2 S. P. TANK CO2 1 ----- 0.1 M3/HR N/B PIPE 3 HOT WATER

SET STEAM 2.1 70 KG/HR 120 KG/HR 1.5 N/B PIPE

4 C.I.P./S.L. TANK STEAM 2.1 ------ 100 KG/HR 1 N/B PIPE 5 HEAT

EXCHANGER GLYCOL

IN 3.0 70 HL/HR 100 HL/HR 1.5 N/B PIPE -2.2 DEG C

6 HEATEXCHANGER

GLYCOL OUT

2.4 70 HL/HR 50 HL/HR 1.5 N/B PIPE 3.3 DEG C

7 C.I.P./S.L. TANK WATER 2.8 ------ 50 HL/HR 1 N/B PIPE 8 HOT WATER

SET WATER 2.8 ------ ------ N/B PIPE TOP UP

9 PASTEURIZER AIR 5.7 ------ 0.3 M3/HR N/B PIPE 10 PASTEURIZER POWER 480-3-60 20 AMP 11 C.I.P./S.L. TANK C.I.P.

RETURN ------ ------ ------- 1.5 O/D TUBE FROM

FILLER 12 C.I.P./S.L. TANK CAUSTIC ------ ------ ------ N/B PIPE DOSING 13 PASTEURIZER PRODUCT

OUT 1 50 HL/HL 50 HL/HR 1.5 O/D TUBE

14 PASTEURIZER C.I.P.RETURN

------- ------ ------ 1.5 O/D TUBE BEER SUPPLY MAIN

An Air Dryer will remove moisture from compressed air to a certain degree of dryness and this is referred to as pressure dew point. Different types of dryers can achieve different dew points and, for the most part, the drier the air needs to be, the more expensive it is to dry

Refrigerated Dryers condense the moisture out of the air and drain it away as liquid. They are limited to about 35 F because the water would freeze if it got any colder.

Desiccant Dryers adsorb the moisture in the compressed air and remove it while still suspended as vapor. They are typically applied at about -40 F, but can get to -100 and below.

Membrane Dryers use permeability to separate the moisture from the air and can also achieve low dew points.

The selection is made on personal preference, the dryness required, and cost, which should include operating and electrical or utility costs.

Reproduced in part from the web site of:

Gulf Atlantic Equipment, Co., Jacksonville, Florida. 904-636-8555 Fax: 904-636-8554 2006


CYCLE TIMES V

SEE FP PROGRAM & CONTROL PHILOSOPHY

SECTIONS FOR INFORMATION


FLOW DIAGRAM W


CONTROL PHILOSOPHY X

CONTROL PHILOSOPHY AUTOMATIC FLASH PASTEURIZER

PROCESS & PACKAGING, INC. 2008 1 of 15

AUTOMATIC FLASH PASTEURIZATION SYSTEM CONTROL PHILOSOPHY

Project: Automatic Flash Pasteurization System Customer: Job Number: Revision:

Originator......................... Name: Jeffrey Gunn Title: President

This is an unpublished work, the copyright of which vests in IDD Process & Packaging Inc. All rights reserved. This document and the information contained herein is supplied without liability for errors or omissions and no part may be reproduced, used or disclosed except as authorized by contract or IDDs written permission. The copyright and the foregoing restrictions and/or reproduction, use and disclosure extend to all media in which this information maybe embodied.

Generic



INDEX: Startup Sequence ------------------------------------------- Page 3 Alarm Sequence 1 ----------------------------------------------- Page 5

- Product over temperature on holding tube (RTD1) - Flow Meter (FM1) low flow - SPT HL probe condition

Alarm Sequence 2 ------------------------------------------ Page 7 - SPT UHL Condition (DP Failure)

Alarm Sequence 3------------------------------------------- Page 8

- Under temperature alarm - Flow Meter (FM1) high flow

Alarm Sequence 4 ------------------------------------------ Page 9

- SPT ULL probe becomes uncovered during production forward flow

Runoff Sequence ------------------------------------------- Page 10 Shutdown Sequence --------------------------------------- Page 12 Abbreviation descriptions --------------------------------- Page 14 Flow Diagram ---------------------------------------------- Page 15



START UP SEQUENCE:

Start-Up to be commenced only after CIP and Hot Water

and/or Oxine Water Sterilize sequence

NOTE: All sequences described below are automatic unless preceded with Operator

Reference attached Flow Diagram Open V7 until water exits through PRV1 to drain. Open AV6 to fill SL/CIP Tank Operator - select MENU then VALVE SCREEN and turn on AV2 & AV4. Select MENU

then PUMPS SCREEN and turn on Main Product Pump (P1), and Hot Water Pump (P3) to place pasteurizer into water recirculation.

Operator - select MENU then TEMP. SELECT SCREEN and select either target

pasteurize or target CIP temperature. If necessary adjustment of setpoint can be made by selecting the TEMPERATURE ADJUST SCREEN and adjusting the appropriate target temperature.

When AV2 & AV4 are shown open, Main Product Pump (P1) running, FM1 flow indication,

Hot Water Recirculation Pump (P3) running & SL Tank LL probe is covered. System waits 1 min. to check system stability; Main Screen STATUS displays UNSTABILIZED or STABILIZED depending on temperature stability.

NOTE: A STABILIZED condition must be shown for system to be ready for automatic startup. NOTE: Flow rate and chase times are preset at time of commissioning. Operator - select MENU then STARTUP. AV1 opens. When AV1 is open; AV2 closes. When AV2 is closed; Start Product chase of water to SL/CIP Tank timer.



Main screen displays PROD/WTR TO SLT. When the timer times out; AV5 opens. When AV5 is open; AV4 closes. When AV4 is closed; Start Product chase of water/product interface to Drain timer. Main screen displays PROD/WTR TO DRAIN. When the timer times out; AV3 opens. When AV3 is open; AV5 closes. When AV5 is closed; Main screen displays FORWARD FLOW NOTE: Manual valve V9 on AV5 drain line is partially closed and set to control flow rate to equal

the resistance of the SPT back pressure of 13 to 15 PSIG When Low Level point in SPT is reached; Product Boost Pump (P2) starts. (Operator must first turn Product on at the PUMPS screen) If CIP/SL Tank LL probe is uncovered AV6 opens. AV6 closes when CIP/SL Tank HL probe becomes covered.



ALARM SEQUENCE 1

DURING PRODUCTION / FORWARD FLOW. Alarm Conditions: Product over temperature on holding tube (RTD 1). Flow Meter low flow (FM1). SPT High Level Alarm condition.

Audible alarm on. Operator to press ALARM ACCEPT and confirm type of alarm under ALARMS on the

Main Display Screen. AV2 opens. When AV2 is open; AV1 closes. When AV1 is closed; Main screen displays WTR/PROD TO SPT. Start water chase timer of product to the SPT When the timer times out; AV5 opens. When AV5 is open; AV3 closes. Main screen displays WTR/PROD TO DRAIN. Start water flush timer. Product/Water interface flushed to drain. Water flush timer times out. AV4 opens. When AV4 is open;



AV5 closes. When AV5 is closed; Main screen displays WATER RECIRCULATION. When the alarm has cleared and the system has stabilized for 1 min., remain in water

recirculation until the level in the SPT falls below low level.

AV1 opens. When AV1 is open; AV2 closes. When AV2 is closed; Start Product chase of water to CIP/SL Tank timer. Main screen displays PROD/WTR TO SLT. When the timer times out; AV5 opens. When AV5 is open; AV4 closes. When AV4 is closed; Start product chase of water to drain timer. Product chases Water/Product interface to drain. Main screen displays PROD/WTR TO DRAIN. When the timer times out; AV3 opens When AV3 is open;



When AV5 closes. When AV5 is closed; Main screen displays FORWARD FLOW. If C I P/S L Tank LL Probe in uncovered AV6 opens until it is covered

ALARM SEQUENCE 2 DURING PRODUCTION / FORWARD FLOW.

Alarm Condition: SPT - DP Cell Failure Alarm.

Audible alarm on. Operator to press ALARM ACCEPT and confirm type of alarm under ALARMS on the

Main Display Screen. AV5 opens. When AV5 is open; AV3 closes. When AV3 is closed; AV2 opens. When AV2 is open; AV1 closes. When AV1 is closed; Main screen displays WTR/PROD TO DRAIN. Start water chase timer of product to drain. When the timer times out; AV4 opens. When AV4 is open;



AV5 closes. When AV5 is closed. Main screen displays WATER RECIRCULATION. Operator to wait until SPT empties below ULL point. Operator to go to MENU screen then press SHUTDOWN to repair DP Cell failure. When problem is resoved repeat startup sequence.

ALARM SEQUENCE 3

DURING PRODUCTION / FORWARD FLOW.

Alarm Conditions: Under temperature alarm (RTD 1) Flow Meter (FM1) high flow. Audible alarm on. Operator to press ALARM ACCEPT and confirm type of alarm under ALARMS on the

Main Display Screen. The Glycol proportional valves close. Operator to close glycol manual isolation valve & open glycol vent V30. AV5 opens. When AV5 is open; AV3 closes. When AV3 is closed; AV2 opens. When AV2 is open; AV1 closes. When AV1 is closed;



Main screen displays WTR/PROD TO DRAIN. Start water chase of product to drain timer. When the timer times out; AV4 opens. When AV4 is open; AV5 closes. When AV5 is closed; Interrupt AV6 top up of CIP/SLT during this sequence: Main screen displays WATER RECIRCULATION. Operator selects MENU then SHUTDOWN Operator to repair alarm condition. Operator commences with manual re-sterilize and CIP procedure.

ALARM SEQUENCE 4

DURING PRODUCTION / FORWARD FLOW.

Alarm Condition: SPT Ultra Low Level (ULL) reached during production/forward flow. Product Boost Pump (P2) stops. Audible alarm on. Operator to press ALARM ACCEPT and confirm type of alarm under ALARMSon the

Main Display Screen. P2 re-starts when level in SPT reaches Low Level.



RUNOFF SEQUENCE:

At any time during production forward flow the operator can run out the remaining product in the pipework to the SPT for the end of production, brand change or temporary interrupt of pasteurizing as follows: Operator to select MENU then RUNOFF from the display. AV2 opens. When AV2 is open; AV1 closes. When AV1 is closed; Main screen displays WTR/PROD to SPT. Start water chase timer of product to the SPT When the timer times out; AV5 opens. When AV5 is open; AV3 closes. When AV3 is closed; Start water flush timer. Product/water interface flushed to drain; main screen displays WTR/PROD TO DRAIN. Water flush timer times out. AV4 opens. When AV4 is open; AV5 closes. When AV5 is closed.



Main screen displays RUNOFF. (This means system is water recirculation) NOTE: If desired at this point, the operator can shut down the system by pressing SHUTDOWN, or press RE-START to continue with production. If SHUTDOWN is selected please see Shutdown, end of production & flush out sequence. NOTE: To re-start production / forward flow the operator can, at any time complete the following: From the MENU screen press RE-START When the CIP/SL Tank LL probe is covered; AV1 opens. When AV1 is open; AV2 closes. When AV2 is closed; Start Product chase of water to CIP/SL Tank timer. Main screen displays PROD/WTR TO SLT. When the timer times out; AV5 opens. When AV5 is open; AV4 closes. When AV4 is closed; Product/water interface chased to drain. Start Product chase of water to Drain timer. Main screen displays PROD/WTR TO DRAIN. When the timer times out; AV3 opens.



When AV3 is open;opens AV5 closes. When AV5 is open; Main screen displays FORWARD FLOW.

SHUTDOWN SEQUENCE: End of production & flush out.

NOTE: All Sequences below are manual and are performed by the Operator.

NOTE: System must indicate WATER RECIRCULATION" on Main Screen. From the MENU screen select SHUTDOWN. The Hot Water Recirculation Pump (P3) will

stop. The steam and glycol proportional valves will be driven closed. Close the steam and glycol supplies to the HWS and PHE respectively. NOTE: Selecting shutdown on the display will produce the CIP screen which is for manual control of all auto valvesAV and pumps from this point on. Turn off the CO2 supply to the SPT Slowly open SPT valve V13 to drain and de-pressurize the tank and pipework. Open SPT valve V11. Partially open SPT valve V10. Set filling line equipment up for CIP Close CIP/SL Tank valve V15. Open CIP/SL Tank valve V14. Check the CIP/SL Tank is full; if not open AV6 until the tank is full. Open and close AV5 several times to rinse the valve. Open AV3.



Close AV4 When the level in the S.P.T reaches Low Level Open V12 Start the Product Boost Pump (P2) When clean water is detected at the CIP/SL Tank V14 drain Open CIP/SL Tank V15 Close CIP/SL Tank V14 Stop all pumps and close all auto valves. End of Flush Out and Shut Down sequence.



ABBREVIATION DESCRIPTION SPT ----------------- STERILE PRODUCT TANK CIP/SL Tank ------- CLEANING IN PLACE / STERILE LIQUOR TANK HWR ---------------- HOT WATER RECIRCULATION P1 -------------------- MAIN PRODUCT PUMP (MPP) P2 -------------------- PRODUCT BOOST PUMP (PBP) P3 -------------------- HOT WATER RECIRCULATION PUMP (HWRP) AV ------------------- AUTO VALVES (1 THRU 6) V --------------------- MANUAL VALVES (7 THRU 18) FM1 ----------------- FLOW METER RTD1 ---------------- RESISTANCE THERMOMETER (PASTEURIZATION TEMP) RTD2 ---------------- RESISTANCE THERMOMETER (PASTEURIZER OUTLET TEMP) PHE ------------------ PLATE HEAT EXCHANGER CIP ------------------- CLEAN IN PLACE PRV ------------------ PRESSURE RELIEF VALVE (HWR) PRV/AVV ----------- PRESSURE RELIEF/ANTI-VACUUM VALVE (SPT) FCV1 ----------------- FLOW CONTROL VALVE (MPP OUTLET) FCV2 ----------------- FLOW CONTROL VALVE (PHE OUTLET) PCV1 & 2 ------------ PROPORTIONAL CONTROL VALVES (STEAM AND GLYCOL) TCV1 ----------------- THERMOSTATIC CONTROL VALVE (STEAM) LL --------------------- CIP/SL TANK LOW LEVEL PROBE HL --------------------- CIP/SL TANK HIGH LEVEL PROBE


PROGRAM LISTING Y

Program Loaded into PLC & Fully Tested

Program Listing Copy is on File


APPENDIX Z

What is Pasteurization and how is it defined ?

Louis Pasteur (1822 - 1895), the father of microbiology and pasteurization, found th

Documents

Manual Flash Pasteurizacion