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Protein precipitation

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691:(pI) is the pH of a solution at which the net primary charge of a protein becomes zero. At a solution pH that is above the pI the surface of the protein is predominantly negatively charged and therefore like-charged molecules will exhibit repulsive forces. Likewise, at a solution pH that is below the pI, the surface of the protein is predominantly positively charged and repulsion between proteins occurs. However, at the pI the negative and positive charges cancel, repulsive electrostatic forces are reduced and the attraction forces predominate. The attraction forces will cause aggregation and precipitation. The pI of most proteins is in the pH range of 4–6. Mineral acids, such as 84:
increasing concentration of co-ions. The presence of these solvation layers cause the protein to have fewer ionic interactions with other proteins and decreases the likelihood of aggregation. Repulsive electrostatic forces also form when proteins are dissolved in water. Water forms a solvation layer around the hydrophilic surface residues of a protein. Water establishes a concentration gradient around the protein, with the highest concentration at the protein surface. This water network has a damping effect on the attractive forces between proteins.
158:. This phase occurs at a slower rate. During the final step, called aging in a shear field, the precipitate particles repeatedly collide and stick, then break apart, until a stable mean particle size is reached, which is dependent upon individual proteins. The mechanical strength of the protein particles correlates with the product of the mean shear rate and the aging time, which is known as the Camp number. Aging helps particles withstand the fluid shear forces encountered in pumps and centrifuge feed zones without reducing in size. 91: 122:. For example, basic residues on a protein can have electrostatic interactions with acidic residues on another protein. However, solvation by ions in an electrolytic solution or water will decrease protein–protein attractive forces. Therefore, to precipitate or induce accumulation of proteins, the hydration layer around the protein should be reduced. The purpose of the added reagents in protein precipitation is to reduce the hydration layer. 851:, are frequently used to precipitate proteins because they have low flammability and are less likely to denature biomaterials than isoelectric precipitation. These polymers in solution attract water molecules away from the solvation layer around the protein. This increases the protein–protein interactions and enhances precipitation. For the specific case of polyethylene glycol, precipitation can be modeled by the equation: 672: 129: 103: 178:, compresses the solvation layer and increases protein–protein interactions. As the salt concentration of a solution is increased, the charges on the surface of the protein interact with the salt, not the water, thereby exposing hydrophobic patches on the protein surface and causing the protein to fall out of solution (aggregate and precipitate). 298:
protein aggregation and precipitation. Chaotropes or "water structure breakers," have the opposite effect of Kosmotropes. These salts promote an increase in the solvation layer around a protein. The effectiveness of the kosmotropic salts in precipitating proteins follows the order of the Hofmeister series:
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to a solution may cause proteins in the solution to precipitate. The solvation layer around the protein will decrease as the organic solvent progressively displaces water from the protein surface and binds it in hydration layers around the organic solvent molecules. With smaller hydration layers, the
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content on the surface have low solubility in an aqueous solvent. Charged and polar surface residues interact with ionic groups in the solvent and increase the solubility of a protein. Knowledge of a protein's amino acid composition will aid in determining an ideal precipitation solvent and methods.
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Protein precipitate formation occurs in a stepwise process. First, a precipitating agent is added and the solution is steadily mixed. Mixing causes the precipitant and protein to collide. Enough mixing time is required for molecules to diffuse across the fluid eddies. Next, proteins undergo a
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depend on the pH of the solution. Anionic polyelectrolytes are used at pH values less than the isoelectric point. Cationic polyelectrolytes are at pH values above the pI. It is important to note that an excess of polyelectrolytes will cause the precipitate to dissolve back into the solution. An
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Kosmotropes or "water structure stabilizers" are salts which promote the dissipation / dispersion of water from the solvation layer around a protein. Hydrophobic patches are then exposed on the protein's surface, and they interact with hydrophobic patches on other proteins. These salts enhance
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migrate towards charged surface residues on the protein, forming a rigid matrix of counterions on the protein's surface. Next to this layer is another solvation layer that is less rigid and, as one moves away from the protein surface, contains a decreasing concentration of counterions and an
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caused by the mineral acids. For this reason isoelectric point precipitation is most often used to precipitate contaminant proteins, rather than the target protein. The precipitation of casein during cheesemaking, or during production of sodium caseinate, is an isoelectric precipitation.
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as they move though the tubes of the reactor. Turbulent flow is promoted through wire mesh inserts in the tube. The tubular reactor does not require moving mechanical parts and is inexpensive to build. However, the reactor can become impractically long if the particles aggregate slowly.
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Batch reactors are the simplest type of precipitation reactor. The precipitating agent is slowly added to the protein solution under mixing. The aggregating protein particles tend to be compact and regular in shape. Since the particles are exposed to a wide range of
283:= Absolute temperature. When water molecules in the rigid solvation layer are brought back into the bulk phase through interactions with the added salt, their greater freedom of movement causes a significant increase in their entropy. Thus, Δ 635: 149:
phase, where submicroscopic sized protein aggregates, or particles, are generated. Growth of these particles is under Brownian diffusion control. Once the particles reach a critical size (0.1 ÎĽm to 10 ÎĽm for high and low
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In tubular reactors, feed protein solution and the precipitating reagent are contacted in a zone of efficient mixing then fed into long tubes where precipitation takes place. The fluid in volume elements approach
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is the salt concentration. The ideal salt for protein precipitation is most effective for a particular amino acid composition, inexpensive, non-buffering, and non-polluting. The most commonly used salt is
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amino acid residues on the protein's surface. Hydrophobic residues predominantly occur in the globular protein core, but some exist in patches on the surface. Proteins that have high hydrophobic
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when the right concentration of the salt is reached in solution. The hydrophobic patches on the protein surface generate highly ordered water shells. This results in a small decrease in
1130: 909: 661:. There is a low variation in salting out over temperatures 0 Â°C to 30 Â°C. Protein precipitates left in the salt solution can remain stable for years-protected from 528: 725:
proteins can aggregate by attractive electrostatic and dipole forces. Important parameters to consider are temperature, which should be less than 0 Â°C to avoid
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solubility curve of the type shown. The relationship between the solubility of a protein and increasing ionic strength of the solution can be represented by the
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solution. These repulsive forces between proteins prevent aggregation and facilitate dissolution. Upon dissolution in an electrolyte solution, solvent
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industry protein precipitation is used to eliminate contaminants commonly contained in blood. The underlying mechanism of precipitation is to alter the
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fields, respectively), by diffusive addition of individual protein molecules to it, they continue to grow by colliding into each other and sticking or
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Zellner; et al. (June 2005). "Quantitative validation of different protein precipitation methods in proteome analysis of blood platelets".
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There are numerous industrial scaled reactors than can be used to precipitate large amounts of proteins, such as recombinant
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for plasma protein fractionation relies on solvent precipitation with ethanol to isolate individual plasma proteins.
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a clinical application for the use of methanol as a protein precipitating agent is in the estimation of bilirubin.
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and polyphosphates can form extended networks between protein molecules in solution. The effectiveness of these
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are used as precipitants. The greatest disadvantage to isoelectric point precipitation is the irreversible
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with a continuous flow of reactants and products in a well-mixed tank. Fresh protein feed contacts
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example of polyelectrolyte flocculation is the removal of protein cloud from beer wort using
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is the most common method used to precipitate a protein. Addition of a neutral salt, such as
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of the ordered water molecules relative to the molecules in the bulk solution. The overall
1062: 630:{\displaystyle I={\begin{matrix}{\frac {1}{2}}\end{matrix}}\sum _{i=1}^{n}c_{i}z_{i}^{2}} 1224: 1046: 737:
the relationship between the dielectric constant and protein solubility is given by:
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Dispersive or attractive forces exist between proteins through permanent and induced
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for a long period of time, they tend to be compact, dense and mechanically stable.
1077: 826: 729:, pH and protein concentration in solution. Miscible organic solvents decrease the 692: 155: 1025: 662: 171: 76: 59: 55: 548:
is the ionic strength of the solution, which is attributed to the added salt.
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of water, which in effect allows two proteins to come close together. At the
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that already contains precipitate particles and the precipitation reagents.
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Metal salts can be used at low concentrations to precipitate enzymes and
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Repulsive electrostatic forces form when proteins are dissolved in an
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is a constant that relates to the dielectric constant of water. The
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of proteins in aqueous buffers depends on the distribution of
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and bacterial contamination by the high salt concentrations.
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of biological products in order to concentrate proteins and
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becomes negative and precipitation occurs spontaneously.
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Bioseparations: downstream processing for biotechnology.
462:{\displaystyle \mathrm {NH_{4}^{+}>K^{+}>Na^{+}} } 564: 934: 860: 746: 556: 494: 409: 307: 223: 27:
them from various contaminants. For example, in the
35:of the solvent, more specifically, by lowering the 983: 903: 799: 629: 522: 461: 392: 256: 925:is a protein–polymer interaction coefficient and 1203:. John Wiley & Sons, Inc. New York, NY 2001. 1196:(2nd Edition). Prentice Hall International. 2001 1217:John Wiley & Sons, Inc. New York, NY 1988. 1210:John Wiley & Sons, Inc. New York, NY 1994. 921:is a protein–protein interaction coefficient, 821:is the dielectric constant of the mixture and 477:The decrease in protein solubility follows a 8: 1024:, carboxymethylcellulose, polyacrylic acid, 257:{\displaystyle \Delta G=\Delta H-T\Delta S.} 1189:Oxford University Press. New York, NY 2003. 984:{\displaystyle x=(\mu _{i}-\mu _{i}^{0})RT} 800:{\displaystyle \log S=k/e^{2}+\log S^{0}\,} 966: 961: 948: 933: 900: 859: 796: 790: 771: 762: 745: 621: 616: 606: 596: 585: 567: 563: 555: 519: 493: 452: 436: 423: 418: 410: 408: 383: 367: 345: 340: 321: 316: 308: 306: 222: 39:of the solute by addition of a reagent. 1187:Bioseparations Science and Engineering. 1122: 1098:Continuous stirred tank reactors (CSTR) 667: 275:= Enthalpy change upon precipitation, Δ 124: 86: 1194:Bioprocess Engineering: Basic Concepts 1053:frequently used are Ca, Mg, Mn or Fe. 279:= Entropy change upon precipitation, 7: 708:Precipitation with miscible solvents 647:is the ion charge of the salt and 449: 445: 433: 415: 411: 380: 376: 364: 360: 357: 337: 333: 313: 309: 245: 233: 224: 182:Energetics involved in salting out 14: 1049:from solutions. Polyvalent metal 1017:Flocculation by polyelectrolytes 904:{\displaystyle \ln(S)+pS=X-aC\,} 670: 544:is a salt-specific constant and 127: 101: 89: 42:Biochemical laboratory technique 972: 941: 917:is the polymer concentration, 873: 867: 836:Non-ionic hydrophilic polymers 114:Attractive electrostatic force 1: 1013:is the absolute temperature. 536:= solubility of the protein, 523:{\displaystyle \log S=B-KI\,} 71:Repulsive electrostatic force 813:is an extrapolated value of 198:, and a larger decrease in 1247: 1201:Bioseparations Engineering 683:Isoelectric precipitation 540:is idealized solubility, 1041:Polyvalent metallic ions 1208:Bioprocess Engineering. 473:Salting out in practice 271:= Free energy change, Δ 1171:10.1002/elps.200410262 1057:Precipitation reactors 1007:universal gas constant 985: 905: 801: 631: 601: 524: 463: 394: 258: 986: 906: 802: 632: 581: 525: 464: 395: 259: 140:Precipitate formation 96:Ionic solvation layer 21:downstream processing 17:Protein precipitation 932: 858: 849:polyethylene glycols 744: 554: 492: 469:least precipitation 407: 400:least precipitation 305: 221: 971: 731:dielectric constant 626: 428: 403:Most precipitation 353: 329: 301:Most precipitation 188:spontaneous process 33:solvation potential 1137:on 18 October 2006 999:chemical potential 981: 957: 901: 797: 627: 612: 579: 520: 459: 414: 390: 336: 312: 254: 46:General principles 19:is widely used in 1213:Belter, Paul A. 1185:Harrison et al., 735:isoelectric point 716:solvents such as 689:isoelectric point 575: 292:Hofmeister series 186:Salting out is a 1238: 1182: 1147: 1146: 1144: 1142: 1133:. Archived from 1127: 1105:reactors run at 1084:Tubular reactors 1065:from a solution. 1030:polyelectrolytes 1001:of component I, 990: 988: 987: 982: 970: 965: 953: 952: 910: 908: 907: 902: 806: 804: 803: 798: 795: 794: 776: 775: 766: 677:Solubility curve 674: 659:ammonium sulfate 636: 634: 633: 628: 625: 620: 611: 610: 600: 595: 580: 576: 568: 529: 527: 526: 521: 468: 466: 465: 460: 458: 457: 456: 441: 440: 427: 422: 399: 397: 396: 391: 389: 388: 387: 372: 371: 352: 344: 328: 320: 263: 261: 260: 255: 176:ammonium sulfate 131: 105: 93: 1246: 1245: 1241: 1240: 1239: 1237: 1236: 1235: 1221: 1220: 1192:Shuler et al., 1158:Electrophoresis 1154: 1151: 1150: 1140: 1138: 1129: 1128: 1124: 1119: 1100: 1086: 1073: 1063:DNA polymerases 1059: 1043: 1019: 944: 930: 929: 856: 855: 838: 786: 767: 742: 741: 710: 685: 678: 675: 655: 646: 602: 578: 577: 552: 551: 490: 489: 475: 448: 432: 405: 404: 379: 363: 303: 302: 295: 219: 218: 184: 169: 164: 142: 135: 134:Hydration layer 132: 116: 109: 108:Hydration layer 106: 97: 94: 73: 48: 43: 12: 11: 5: 1244: 1242: 1234: 1233: 1223: 1222: 1219: 1218: 1211: 1204: 1197: 1190: 1183: 1165:(12): 2481–9. 1149: 1148: 1121: 1120: 1118: 1115: 1099: 1096: 1085: 1082: 1078:shear stresses 1072: 1071:Batch reactors 1069: 1058: 1055: 1042: 1039: 1018: 1015: 992: 991: 980: 977: 974: 969: 964: 960: 956: 951: 947: 943: 940: 937: 912: 911: 899: 896: 893: 890: 887: 884: 881: 878: 875: 872: 869: 866: 863: 837: 834: 808: 807: 793: 789: 785: 782: 779: 774: 770: 765: 761: 758: 755: 752: 749: 709: 706: 684: 681: 680: 679: 676: 669: 651: 642: 624: 619: 615: 609: 605: 599: 594: 591: 588: 584: 574: 571: 566: 565: 562: 559: 531: 530: 518: 515: 512: 509: 506: 503: 500: 497: 474: 471: 455: 451: 447: 444: 439: 435: 431: 426: 421: 417: 413: 386: 382: 378: 375: 370: 366: 362: 359: 356: 351: 348: 343: 339: 335: 332: 327: 324: 319: 315: 311: 294: 289: 265: 264: 253: 250: 247: 244: 241: 238: 235: 232: 229: 226: 183: 180: 168: 165: 163: 160: 141: 138: 137: 136: 133: 126: 115: 112: 111: 110: 107: 100: 98: 95: 88: 72: 69: 47: 44: 41: 13: 10: 9: 6: 4: 3: 2: 1243: 1232: 1231:Biotechnology 1229: 1228: 1226: 1216: 1212: 1209: 1205: 1202: 1198: 1195: 1191: 1188: 1184: 1180: 1176: 1172: 1168: 1164: 1160: 1159: 1153: 1152: 1136: 1132: 1126: 1123: 1116: 1114: 1112: 1108: 1104: 1097: 1095: 1092: 1083: 1081: 1079: 1070: 1068: 1067: 1064: 1056: 1054: 1052: 1048: 1047:nucleic acids 1040: 1038: 1036: 1031: 1027: 1023: 1016: 1014: 1012: 1008: 1004: 1000: 996: 978: 975: 967: 962: 958: 954: 949: 945: 938: 935: 928: 927: 926: 924: 920: 916: 897: 894: 891: 888: 885: 882: 879: 876: 870: 864: 861: 854: 853: 852: 850: 846: 842: 835: 833: 830: 828: 824: 820: 816: 812: 791: 787: 783: 780: 777: 772: 768: 763: 759: 756: 753: 750: 747: 740: 739: 738: 736: 732: 728: 723: 719: 715: 707: 705: 702: 698: 697:sulfuric acid 694: 690: 682: 673: 668: 666: 664: 660: 654: 650: 645: 641: 637: 622: 617: 613: 607: 603: 597: 592: 589: 586: 582: 572: 569: 560: 557: 549: 547: 543: 539: 535: 516: 513: 510: 507: 504: 501: 498: 495: 488: 487: 486: 484: 480: 472: 470: 453: 442: 437: 429: 424: 419: 401: 384: 373: 368: 354: 349: 346: 341: 330: 325: 322: 317: 299: 293: 290: 288: 286: 282: 278: 274: 270: 251: 248: 242: 239: 236: 230: 227: 217: 216: 215: 213: 209: 205: 201: 197: 193: 189: 181: 179: 177: 173: 166: 161: 159: 157: 153: 148: 139: 130: 125: 123: 121: 113: 104: 99: 92: 87: 85: 82: 78: 70: 68: 65: 61: 57: 53: 45: 40: 38: 34: 30: 29:biotechnology 26: 22: 18: 1214: 1207: 1200: 1193: 1186: 1162: 1156: 1139:. Retrieved 1135:the original 1125: 1107:steady state 1101: 1087: 1074: 1060: 1044: 1020: 1010: 1002: 994: 993: 922: 918: 914: 913: 839: 831: 827:Cohn process 822: 818: 814: 810: 809: 727:denaturation 712:Addition of 711: 701:denaturation 693:hydrochloric 686: 652: 648: 643: 639: 638: 550: 545: 541: 537: 533: 532: 476: 402: 300: 296: 284: 280: 276: 272: 268: 266: 211: 203: 195: 185: 170: 156:flocculating 143: 117: 74: 49: 16: 15: 1141:14 December 1026:tannic acid 663:proteolysis 208:free energy 172:Salting out 167:Salting out 81:counterions 77:electrolyte 60:hydrophobic 56:hydrophilic 1206:Lydersen. 1117:References 1035:Irish moss 843:, such as 485:equation: 479:normalized 147:nucleation 64:amino acid 52:solubility 37:solubility 1199:Ladisch. 1091:plug flow 959:μ 955:− 946:μ 892:− 865:⁡ 784:⁡ 751:⁡ 583:∑ 511:− 499:⁡ 385:− 369:− 350:− 326:− 246:Δ 240:− 234:Δ 225:Δ 210:change, Δ 1225:Category 1179:15895463 1022:Alginate 845:dextrans 841:Polymers 722:methanol 714:miscible 192:enthalpy 1005:is the 997:is the 718:ethanol 200:entropy 162:Methods 120:dipoles 1177:  1111:slurry 25:purify 152:shear 1175:PMID 1143:2006 1103:CSTR 1051:ions 1009:and 847:and 695:and 687:The 483:Cohn 443:> 430:> 374:> 355:> 331:> 58:and 50:The 1167:doi 781:log 748:log 720:or 496:log 202:, Δ 194:, Δ 1227:: 1173:. 1163:26 1161:. 1037:. 862:ln 817:, 204:S, 1181:. 1169:: 1145:. 1011:T 1003:R 995:ÎĽ 979:T 976:R 973:) 968:0 963:i 950:i 942:( 939:= 936:x 923:a 919:P 915:C 898:C 895:a 889:X 886:= 883:S 880:p 877:+ 874:) 871:S 868:( 823:k 819:e 815:S 811:S 792:0 788:S 778:+ 773:2 769:e 764:/ 760:k 757:= 754:S 653:i 649:c 644:i 640:z 623:2 618:i 614:z 608:i 604:c 598:n 593:1 590:= 587:i 573:2 570:1 561:= 558:I 546:I 542:K 538:B 534:S 517:I 514:K 508:B 505:= 502:S 454:+ 450:a 446:N 438:+ 434:K 425:+ 420:4 416:H 412:N 381:l 377:C 365:O 361:O 358:C 347:2 342:4 338:O 334:S 323:3 318:4 314:O 310:P 285:G 281:T 277:S 273:H 269:G 267:Δ 252:. 249:S 243:T 237:H 231:= 228:G 212:G 196:H

Index

downstream processing
purify
biotechnology
solvation potential
solubility
solubility
hydrophilic
hydrophobic
amino acid
electrolyte
counterions
Ionic solvation layer
Hydration layer
dipoles
Hydration layer
nucleation
shear
flocculating
Salting out
ammonium sulfate
spontaneous process
enthalpy
entropy
free energy
Hofmeister series
normalized
Cohn
ammonium sulfate
proteolysis
Solubility curve

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