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Waste Treatment for the CIP System 319 FIGURE 2 Oversized drain at CIP skid. Source: Courtesy of Lonza Biologics, Portsmouth, NH, U.S.A. delivery frequency (Fig. 4). These acid and base solutions require appropriate operator safety precautions and special containment for their storage tanks. It is common to provide spill containment for 110% of maximum stored volume as well as complete segregation of the acid and base in case of aspill. The reaction caused by aspill of these stored quantities of acid and base could lead to dangerous heat levels generated from the exothermic reaction as well as noxious fumes. The design and installation of equipment to handle the neutralization procedure must give consideration to the following factors: & Spill containment & Segregation of acid and base & Color-coded and labeled piping and fill connections & Metering pumps (with installed spares) Because of the logarithmic nature of the pH scale, adifferent quantity of base is required to adjust the pH from2to 3ascompared to adjusting the pH from5to 6. The quantity of chemical required for neutralization is also affected by: ( i )incoming solution pH, ( ii) type and concentration of CIP chemical used, (iii) type and concentration of neutralization chemical used, ( iv) overall alkalinity of the wastewater stream, ( v )buffering capacity of the wastewater stream, and ( vi) dilution of
320 M M M M Acid caustic Acid caustic TI pH Flow pH pH pH Process/cip Effluent Neutralization Effluent (to city sewer &POTW) Flume (flow measurement) pH Neutralization tank #2 pH Neutralization tank #1 Equalization tank FIGURE 3 Three-tank waste neutralization system. Abbreviations :POTW, publicity operated treatment works. Rauch and Ankers
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Clean-In-Place for Biopharmaceutica
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Informa Healthcare USA, Inc. 52 Van
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iv Preface period, the industry rec
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Preface iii Contents Acknowledgment
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Contributors Barry J. Andersen Seib
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2 the last step of abatch manufactu
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4 Seiberling The vessel capacity ma
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6 Seiberling any two ports. For pur
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8 AWFI (or Any Water) Supply If the
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10 Seiberling program, and through
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12 Seiberling (380 L) for the solut
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14 AWFI CIP skid Drain When steam a
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16 Seiberling products in asingle f
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18 Seiberling The literature began
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2 Project Planning for the CIPable
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Project Planning for CIPable Facili
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3 Water for the CIP System Jay C. A
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Water for the CIP System 43 FIGURE
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Water for the CIP System 45 of clea
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Water for the CIP System 51 WATER U
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54 Time Temperature FIGURE 2 The cl
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56 Classification of Cleaners by pH
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58 [mg/sec] Cleaning velocity C v ,
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60 + - Na O O C CH 2 CH 2 (CH 2 ) n
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62 CH3 -(CH2 ) n -CH2 -O -CH2 -CH2
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64 B C D E FIGURE 17 Capability of
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66 pH 13 pH 7 pH, %, Excess water h
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68 dramatically increased rinsing t
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70 desorption. If the affinity is v
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72 & Cleaning procedure inthe case
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74 effort being performed relativel
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76 Rush & A1000 Lmixing vessel, hav
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78 TABLE 2 Typical Single-Pass Chem
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80 Rush Rinse Volume (Duration) The
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82 Rush Intermediate Drain Objectiv
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84 Rush Final Drain Phase (Gravity)
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86 TABLE 4 Recirculated Chemical Wa
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88 Rush type of soil include fermen
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90 The pre-cleaning process flush w
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92 REFERENCES Rush 1. Howard T, Wie
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94 CIP return (CIPR)-piping to conv
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96 Seiberling provided, generally o
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98 Single-Tank CIP Skid Operational
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100 Single-Tank Bypass or Recycle O
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102 Seiberling Single-Tank Single P
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104 Seiberling installation of an e
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106 Chemical loop AB FE Chemical bl
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108 Chemical loop AB FCV FE Steam C
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CIP supply Transfer line (typical)
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112 Seiberling FIGURE 14 This singl
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114 Seiberling FIGURE 15 This large
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116 Seiberling FIGURE 17 This mini-
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7 CIP System Instrumentation and Co
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CIP System Instrumentation and Cont
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146 Lebowitz should be considered f
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148 Lebowitz barrels and the chemic
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150 Lebowitz Electromagnetic-Operat
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152 Lebowitz FIGURE 5 The venturi o
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154 Chemical pump enclosure Acid AL
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156 Steam Facility acid header Faci
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158 Lebowitz That is to say aweak a
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160 CIP Philosophy The production p
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162 Franks and Seiberling the numbe
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164 Franks and Seiberling Similar s
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166 Franks and Seiberling FIGURE 3
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170 (A) (B) Franks and Seiberling F
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174 The variables that impact the r
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176 There are two guiding concepts
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178 Mezz. Floor(ref.) V-5 1000L CIP
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180 return line piping, substantial
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182 Lebowitz U-bend transfer panels
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184 Lebowitz oriented vertically. T
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186 Lebowitz suction-side port on T
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CIPS loop Primary CIPS CIPSPS CIPS
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190 Lebowitz FIGURE 10 Photo of sma
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192 Drain CIP return Drain Recycle
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11 Materials of Construction and Su
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Materials of Construction and Surfa
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12 Cleanable In-Line Components INT
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Cleanable In-Line Components 213 &
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Cleanable In-Line Components 215 Al
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Cleanable In-Line Components 217 Ex
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Cleanable In-Line Components 219 FI
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Cleanable In-Line Components 221 Tr
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Cleanable In-Line Components 223 it
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Cleanable In-Line Components 229 eq
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Cleanable In-Line Components 231 Th
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Cleanable In-Line Components 233 co
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13 Cleanable Liquids Processing Equ
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Cleanable Liquids Processing Equipm
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1-9 CIPS 2 Plant steam CIPS valves
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258 8. Projectile-type thermometer
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260 Forder control of the drying pr
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262 Forder FIGURE 5 Pharmaceutical
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264 Forder FIGURE 7 Pharmaceutical
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266 FIGURE 9 Pleated filter cartrid
Page 289 and 290: 268 FIGURE 12 Disassembledstainless
Page 291 and 292: 270 The acid wash of 85% phosphoric
Page 293 and 294: 272 FIGURE 17 Sanitary Vbenders. So
Page 295 and 296: 274 one each for the upper, central
Page 297 and 298: 276 CIP VS. TRADITIONAL BOIL-UP MET
Page 299 and 300: 278 Cerulli were not designed to be
Page 301 and 302: 280 by large flanged connections fo
Page 303 and 304: 282 CIP header Once thru CIP soluti
Page 305 and 306: 284 Nozzle Use A Manway B Agitator
Page 307 and 308: 286 3" Stub end w/150# flange 2A 1
Page 309 and 310: 288 In most cases, the pressure dro
Page 311 and 312: 290 CIP fluids Process fluids 1 2 3
Page 313 and 314: 292 A Vent to atm. B M Conical drye
Page 315 and 316: 294 One of the designer’s first t
Page 318 and 319: 16 CIP System Troubleshooting Guide
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Page 336 and 337: 17 Waste Treatment for the CIP Syst
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Page 348 and 349: 18 Commissioning and Qualification
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Page 369 and 370: 348 & Sterilization refers to the r
Page 371 and 372: 350 Lankford All analytical methods
Page 373 and 374: 352 should be based upon scientific
Page 375 and 376: 354 Lankford acleaning validation p
Page 377 and 378: 356 In summary, TOC analysis is are
Page 379 and 380: 358 In-Situ In-situ measurement tec
Page 381 and 382: 360 15. Karen A. Clark, Product Man
Page 383 and 384: 362 Actually, most countries revise
Page 385 and 386: 364 §211.100 Written procedures; d
Page 387 and 388: 366 §211.186 Master production and
Page 389 and 390: 368 Equipment Regulation C.02.005 T
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370 … C.02.004 … 4. Pipework sy
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372 5.20 Schedules and procedures (
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374 TABLE 1 Directives of the Europ
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376 TABLE 5 Cleanability Performanc
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Index Accessibility, 28 Acid cleane
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Index 381 CIP supply flow troublesh
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Index 383 [Cleaning cycle sequences
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Index 385 Flow alarm, no-return, 30
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Index 387 Off skid instrumentation,
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Index 389 Rising stem valves, 223-2
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Index 391 [Troubleshooting] spray c
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