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Drying

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189:, further increasing the driving force for drying. In the falling rate period, as moisture content falls, the solids heat up and the higher temperatures speed up diffusion of water from the interior of the solid to the surface. However, product quality considerations limit the applicable rise to air temperature. Excessively hot air can almost completely dehydrate the solid surface, so that its pores shrink and almost close, leading to crust formation or "case hardening", which is usually undesirable. For instance in wood (timber) drying, air is heated (which speeds up drying) though some steam is also added to it (which hinders drying rate to a certain extent) in order to avoid excessive surface dehydration and product deformation owing to high moisture gradients across timber thickness. 215:, i.e., passed to the gas phase directly from the solid phase, below the melting point of the solvent. It is increasingly applied to dry foods, beyond its already classical pharmaceutical or medical applications. It keeps biological properties of proteins, and retains vitamins and bioactive compounds. Pressure can be reduced by a high vacuum pump (though freeze drying at atmospheric pressure is possible in dry air). If using a vacuum pump, the vapor produced by sublimation is removed from the system by converting it into ice in a condenser, operating at very low temperatures, outside the freeze drying chamber. 273:
darkening, and drying is not only carried out to inhibit microbial growth, but also to avoid browning during storage. Concerning dried fruits, the reduction of moisture acts in combination with its acid and sugar contents to provide protection against microbial growth. Products such as milk powder must be dried to very low moisture contents in order to ensure flowability and avoid caking. This moisture is lower than that required to ensure inhibition to microbial development. Other products as crackers are dried beyond the microbial growth threshold to confer a crispy texture, which is liked by consumers.
145:. If water removal is considerable, the products usually undergo shrinkage and deformation, except in a well-designed freeze-drying process. The drying rate in the falling-rate period is controlled by the rate of removal of moisture or solvent from the interior of the solid being dried and is referred to as being "mass-transfer limited". This is widely noticed in hygroscopic products such as fruits and vegetables, where drying occurs in the falling rate period with the constant drying rate period said to be negligible. 221:(superheated steam drying) involves steam drying of products containing water. This process is feasible because water in the product is boiled off, and joined with the drying medium, increasing its flow. It is usually employed in closed circuit and allows a proportion of latent heat to be recovered by recompression, a feature which is not possible with conventional air drying, for instance. The process has potential for use in foods if carried out at reduced pressure, to lower the boiling point. 755: 20: 137:
individual particles that is being removed. The drying rate during this period is mostly dependent on the rate of heat transfer to the material being dried. Therefore, the maximum achievable drying rate is considered to be heat-transfer limited. If drying is continued, the slope of the curve, the drying rate, becomes less steep (falling rate period) and eventually tends to become nearly horizontal at very long times. The product moisture content is then constant at the "
252: 141:", where it is, in practice, in equilibrium with the dehydrating medium. In the falling-rate period, water migration from the product interior to the surface is mostly by molecular diffusion, i.e. the water flux is proportional to the moisture content gradient. This means that water moves from zones with higher moisture content to zones with lower values, a phenomenon explained by the 154: 69:. This process is often used as a final production step before selling or packaging products. To be considered "dried", the final product must be solid, in the form of a continuous sheet (e.g., paper), long pieces (e.g., wood), particles (e.g., cereal grains or corn flakes) or powder (e.g., sand, salt, washing powder, milk powder). A source of 227:
takes place when materials are dried with unheated forced air, taking advantage of its natural drying potential. The process is slow and weather-dependent, so a wise strategy "fan off-fan on" must be devised considering the following conditions: Air temperature, relative humidity and moisture content
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In some products having a relatively high initial moisture content, an initial linear reduction of the average product moisture content as a function of time may be observed for a limited time, often known as a "constant drying rate period". Usually, in this period, it is surface moisture outside
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Foods are dried to inhibit microbial development and quality decay. However, the extent of drying depends on product end-use. Cereals and oilseeds are dried after harvest to the moisture content that allows microbial stability during storage. Vegetables are blanched before drying to avoid rapid
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Dielectric drying (radiofrequency or microwaves being absorbed inside the material) is the focus of intense research nowadays. It may be used to assist air drying or vacuum drying. Researchers have found that microwave finish drying speeds up the otherwise very low drying rate at the end of the
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In the coatings and adhesives industry, drying is used to cure solvent-based films. In some cases, highly structured films can result. For example, evaporation of solvent from a solution containing helical polymer results in a highly ordered array of squashed toroidal structures.
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and temperature of the material being dried. Grains are increasingly dried with this technique, and the total time (including fan off and on periods) may last from one week to various months, if a winter rest can be tolerated in cold areas.
120:(used, for instance, for manufacturing potato flakes), where a heated surface is used to provide the energy, and aspirators draw the vapor outside the room. In contrast, the mechanical extraction of the solvent, e.g., water, by 285:(as part of timber processing), paper, flax, and washing powder. The first two, owing to their organic origins, may develop mold if insufficiently dried. Another benefit of drying is a reduction in volume and weight. 196:
Indirect or contact drying (heating through a hot wall), as drum drying, vacuum drying. Again, higher wall temperatures will speed up drying but this is limited by product degradation or case-hardening.
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kill, as pathogens can only tolerate a certain dryness level. In addition, drying is required as a process step if the excreta based materials are meant to be incinerated.
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or direct drying). Air heating increases the drying force for heat transfer and accelerates drying. It also reduces air
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classical drying methods. Vacuum microwave drying is used for the US Army's experimental Close Combat Assault Ration.
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and an agent to remove the vapor produced by the process are often involved. In bioproducts like food, grains, and
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In the most common case, a gas stream, e.g., air, applies the heat by convection and carries away the vapor as
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Genskow, L.R.; Beimesch, W.E.; Hecht, J.P.; Kemp, I.C.; Langrish, T.; Schwartzbach, C.; Smith, (F).L. (2007).
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Onwude, Daniel I.; Hashim, Norhashila; Janius, Rimfiel B.; Nawi, Nazmi Mat; Abdan, Khalina (2016-02-04).
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or lyophilization is a drying method where the solvent is frozen prior to drying and is then
804: 689: 634: 330: 218: 166: 8: 624: 390:"drying - definition of drying by the Free Online Dictionary, Thesaurus and Encyclopedia" 361:. Mc Graw Hill Professional. pp. Chapter 12 (Evaporative Cooling and Solids Drying). 544: 684: 580: 514:
Faecal Sludge Management (FSM) book - Systems Approach for Implementation and Operation
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Carroll, Gregory T.; Jongejan, Mahthild G. M.; Pijper, Dirk; Feringa, Ben L. (2010).
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Removal of water or another solvent by evaporation from a solid, semi-solid or liquid
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Among non-food products, some of those that require considerable drying are
799: 784: 674: 644: 476:"Spontaneous generation and patterning of chiral polymeric surface toroids" 441: 190: 31: 27: 19: 389: 774: 629: 335: 282: 198: 117: 82: 54: 288: 161:, the boundary between gas and liquid runs from the triple point to the 794: 779: 669: 604: 549: 491: 475: 294: 251: 182: 121: 109: 62: 877: 260: 105: 834: 809: 594: 413:"Modeling the thin-layer drying of fruits and vegetables: A review" 318: 93: 709: 256: 86: 78: 50: 23: 113: 66: 844: 310: 58: 473: 70: 512:
Strande, L., Ronteltap, M., Brdjanovic, D. (eds.) (2014).
153: 81:, the solvent to be removed is almost invariably water. 410: 49:
process consisting of the removal of water or another
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Comprehensive Reviews in Food Science and Food Safety
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Sludges and fecal materials from sanitation processes
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with drying or considered an extreme form of drying.
128:, is not considered "drying" but rather "draining". 112:), while the vapor thus produced is removed by the 457:"Cooking (and Shrinking) the Modern Combat Ration" 177:The following are some general methods of drying: 911: 565: 165:. Regular drying is the green arrow, while 572: 558: 347: 431: 382: 232: 579: 250: 152: 18: 912: 506: 116:system. Another indirect technique is 553: 317:(UDDT) is a common method to achieve 545:Machinery for drying solid materials 454: 365: 276: 148: 131: 13: 14: 931: 538: 237: 753: 341: 34:in the background and duct for 467: 448: 404: 1: 455:Kord, Tyler (June 29, 2019). 375: 368:Handbook of Industrial Drying 359:Chemical Engineers' Handbook 143:second law of thermodynamics 139:equilibrium moisture content 100:, where heat is supplied by 7: 352:. Woodhead Publishing, Ltd. 324: 315:urine-diverting dry toilets 10: 936: 790:Electrostatic precipitator 265: 96:. Other possibilities are 891: 863: 830:Rotary vacuum-drum filter 762: 751: 587: 201:belongs in this category. 193:belongs in this category. 873:Aqueous two-phase system 695:Liquid–liquid extraction 370:. Boca RatĂłn: CRC Press. 181:Application of hot air ( 770:API oil–water separator 640:Dissolved air flotation 433:10.1111/1541-4337.12196 366:A.S., Mujumdar (1998). 348:Greensmith, M. (1998). 303:sewage treatment plants 246: 735:Solid-phase extraction 523:. IWA Publishing, UK ( 263: 233:Applications of drying 174: 39: 855:Vacuum ceramic filter 850:Sublimation apparatus 655:Electrochromatography 615:Cross-flow filtration 350:Practical Dehydration 259:in the production of 254: 169:is the red arrow and 156: 22: 805:Fractionating column 600:Acid–base extraction 581:Separation processes 331:Dehydration reaction 219:Supercritical drying 167:supercritical drying 625:Cyclonic separation 685:Gravity separation 519:2017-10-14 at the 492:10.1039/c0sc00159g 264: 255:Drying of fish in 225:Natural air drying 175: 40: 30:in a drying room ( 907: 906: 825:Rapid sand filter 720:Recrystallization 700:Electroextraction 660:Electrofiltration 277:Non-food products 187:relative humidity 149:Methods of drying 927: 757: 574: 567: 560: 551: 550: 532: 510: 504: 503: 480:Chemical Science 471: 465: 464: 452: 446: 445: 435: 417: 408: 402: 401: 399: 397: 386: 371: 362: 353: 132:Drying mechanism 935: 934: 930: 929: 928: 926: 925: 924: 910: 909: 908: 903: 887: 865: 859: 820:Protein skimmer 758: 749: 745:Ultrafiltration 725:Reverse osmosis 705:Microfiltration 680:Froth flotation 620:Crystallization 583: 578: 541: 536: 535: 521:Wayback Machine 511: 507: 472: 468: 453: 449: 415: 409: 405: 395: 393: 388: 387: 383: 378: 344: 327: 293:In the area of 291: 279: 270: 249: 240: 235: 151: 134: 75:pharmaceuticals 38:in the ceiling) 17: 12: 11: 5: 933: 923: 922: 905: 904: 902: 901: 899:Unit operation 895: 893: 889: 888: 886: 885: 880: 875: 869: 867: 861: 860: 858: 857: 852: 847: 842: 837: 832: 827: 822: 817: 812: 807: 802: 797: 792: 787: 782: 777: 772: 766: 764: 760: 759: 752: 750: 748: 747: 742: 737: 732: 727: 722: 717: 712: 707: 702: 697: 692: 687: 682: 677: 672: 667: 662: 657: 652: 647: 642: 637: 632: 627: 622: 617: 612: 610:Chromatography 607: 602: 597: 591: 589: 585: 584: 577: 576: 569: 562: 554: 548: 547: 540: 539:External links 537: 534: 533: 505: 466: 447: 426:(3): 599–618. 403: 380: 379: 377: 374: 373: 372: 363: 354: 343: 340: 339: 338: 333: 326: 323: 290: 287: 278: 275: 266:Main article: 248: 245: 239: 238:Film formation 236: 234: 231: 230: 229: 222: 216: 206: 202: 194: 163:critical point 150: 147: 133: 130: 126:centrifugation 15: 9: 6: 4: 3: 2: 932: 921: 918: 917: 915: 900: 897: 896: 894: 890: 884: 881: 879: 876: 874: 871: 870: 868: 862: 856: 853: 851: 848: 846: 843: 841: 840:Spinning cone 838: 836: 833: 831: 828: 826: 823: 821: 818: 816: 815:Mixer-settler 813: 811: 808: 806: 803: 801: 798: 796: 793: 791: 788: 786: 783: 781: 778: 776: 773: 771: 768: 767: 765: 761: 756: 746: 743: 741: 738: 736: 733: 731: 730:Sedimentation 728: 726: 723: 721: 718: 716: 715:Precipitation 713: 711: 708: 706: 703: 701: 698: 696: 693: 691: 688: 686: 683: 681: 678: 676: 673: 671: 668: 666: 663: 661: 658: 656: 653: 651: 648: 646: 643: 641: 638: 636: 633: 631: 628: 626: 623: 621: 618: 616: 613: 611: 608: 606: 603: 601: 598: 596: 593: 592: 590: 586: 582: 575: 570: 568: 563: 561: 556: 555: 552: 546: 543: 542: 530: 529:9781780404738 526: 522: 518: 515: 509: 501: 497: 493: 489: 485: 481: 477: 470: 462: 461:www.yahoo.com 458: 451: 443: 439: 434: 429: 425: 421: 414: 407: 391: 385: 381: 369: 364: 360: 355: 351: 346: 345: 337: 334: 332: 329: 328: 322: 320: 316: 313:collected in 312: 308: 304: 300: 299:sewage sludge 296: 286: 284: 274: 269: 268:Drying (food) 262: 258: 253: 244: 226: 223: 220: 217: 214: 210: 209:Freeze drying 207: 203: 200: 195: 192: 188: 184: 180: 179: 178: 172: 171:freeze drying 168: 164: 160: 159:phase diagram 157:In a typical 155: 146: 144: 140: 129: 127: 123: 119: 115: 111: 107: 103: 99: 98:vacuum drying 95: 90: 88: 84: 80: 76: 72: 68: 64: 60: 56: 52: 48: 47:mass transfer 44: 37: 33: 29: 25: 21: 800:Filter press 785:Depth filter 675:Flocculation 649: 645:Distillation 508: 483: 479: 469: 460: 450: 423: 419: 406: 394:. Retrieved 384: 367: 358: 349: 342:Bibliography 307:fecal sludge 297:, drying of 292: 280: 271: 241: 191:Spray drying 176: 173:is the blue. 135: 91: 42: 41: 32:dehumidifier 28:clothes line 775:Belt filter 740:Sublimation 630:Decantation 336:Drying room 199:Drum drying 118:drum drying 83:Desiccation 55:evaporation 36:ventilation 864:Multiphase 795:Evaporator 780:Centrifuge 670:Filtration 665:Extraction 605:Adsorption 595:Absorption 486:(4): 469. 376:References 295:sanitation 183:convective 122:filtration 110:microwaves 102:conduction 87:synonymous 63:semi-solid 26:hung on a 878:Azeotrope 588:Processes 500:2041-6520 261:stockfish 106:radiation 914:Category 892:Concepts 883:Eutectic 835:Scrubber 810:Leachate 690:Leaching 635:Dialysis 517:Archived 442:33401820 396:23 April 392:. Farlex 325:See also 319:pathogen 213:sublimed 94:humidity 79:vaccines 866:systems 763:Devices 710:Osmosis 257:Lofoten 85:may be 57:from a 51:solvent 24:Laundry 920:Drying 650:Drying 527:  498:  440:  114:vacuum 67:liquid 43:Drying 845:Still 416:(PDF) 311:feces 301:from 77:like 59:solid 45:is a 525:ISBN 496:ISSN 438:PMID 398:2011 283:wood 247:Food 108:(or 71:heat 488:doi 428:doi 309:or 124:or 104:or 65:or 53:by 916:: 494:. 482:. 478:. 459:. 436:. 424:15 422:. 418:. 305:, 61:, 573:e 566:t 559:v 531:) 502:. 490:: 484:1 463:. 444:. 430:: 400:.

Index


Laundry
clothes line
dehumidifier
ventilation
mass transfer
solvent
evaporation
solid
semi-solid
liquid
heat
pharmaceuticals
vaccines
Desiccation
synonymous
humidity
vacuum drying
conduction
radiation
microwaves
vacuum
drum drying
filtration
centrifugation
equilibrium moisture content
second law of thermodynamics

phase diagram
critical point

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