304:+1. Each space has a lower temperature and pressure than the previous space, and the tube walls have intermediate temperatures between the temperatures of the fluids on each side. The pressure in a space cannot be in equilibrium with the temperatures of the walls of both subspaces. It has an intermediate pressure. Then the pressure is too low or the temperature too high in the first subspace, and the water evaporates. In the second subspace, the pressure is too high or the temperature too low, and the vapor condenses. This carries evaporation energy from the warmer first subspace to the colder second subspace. At the second subspace the energy flows by conduction through the tube walls to the colder next space.
278:. It consists of multiple stages or "effects". In each stage the feed water is heated by steam in tubes, usually by spraying saline water onto them. Some of the water evaporates, and this steam flows into the tubes of the next stage (effect), heating and evaporating more water. Each stage essentially reuses the energy from the previous stage, with successively lower temperatures and pressures after each one. There are different configurations, such as forward-feed, backward-feed, etc. Additionally, between stages this steam uses some heat to preheat incoming saline water.
25:
313:
the heat transport per unit surface of the tubes. The energy supplied is reused more times to evaporate more water, but the process takes more time. The amount of water distilled per stage is directly proportional to the amount of energy transport. If the transport is slowed down, one can increase the surface area per stage, i.e. the number and length of the tubes, at the expense of increased installation cost.
287:
327:
The lowest pressure stages need relatively more surface area to achieve the same energy transport across the tube walls. The expense of installing this surface area limits the usefulness of using very low pressures and temperatures in the later stages. Gases dissolved in the feed water may contribute
312:
The thinner the metal in the tubes and the thinner the layers of liquid on either side of the tube walls, the more efficient is the energy transport from space to space. Introducing more stages between the heat source and sink reduces the temperature difference between the spaces and greatly reduces
290:
Schematic of a multiple effect desalination plant. The first stage is at the top. Pink areas are vapor, lighter blue areas are liquid feed water. Stronger turquoise is condensate. It is not shown how feed water enters other stages than the first. F - feed water in. S - heating steam in. C - heating
323:
The first and last stages need external heating and cooling respectively. The amount of heat removed from the last stage must nearly equal the amount of heat supplied to the first stage. For sea water desalination, even the first and warmest stage is typically operated at a temperature below
334:
Condensate (fresh water) from all the tubes in all the stages must be pumped out from the respective pressures of the stages to the ambient pressure. The brine collected at the bottom of the last stage must be pumped out since it has substantially lower pressure than the ambient pressure.
295:
The plant can be seen as a sequence of closed spaces separated by tube walls, with a heat source in one end and a heat sink in the other end. Each space consists of two communicating subspaces, the exterior of the tubes of stage
316:
The salt water collected at the bottom of each stage can be sprayed on the tubes in the next stage, since this water has a suitable temperature and pressure near or slightly above the
331:
External feed water must be supplied to the first stage. The tubes of the first stage are heated using an external source of steam or though any other source of heat.
501:
Panagopoulos, Argyris; Haralambous, Katherine-Joanne; Loizidou, Maria (2019-11-25). "Desalination brine disposal methods and treatment technologies - A review".
320:
and pressure in the next stage. Some of this water will flash into steam as it is released into the next stage at lower pressure than the stage it came from.
418:"Process simulation and techno-economic assessment of a zero liquid discharge/multi-effect desalination/thermal vapor compression (ZLD/MED/TVC) system"
42:
89:
61:
68:
75:
291:
steam out. W - Fresh water (condensate) out. R - brine out. O - coolant in. P - coolant out. VC is the last-stage cooler.
57:
108:
347:
Operates at low temperature (< 70 °C) and at low concentration (< 1.5) to avoid corrosion and scaling
397:
225:
154:
142:
46:
82:
565:
460:
Warsinger, David M.; Mistry, Karan H.; Nayar, Kishor G.; Chung, Hyung Won; Lienhard V, John H. (2015).
392:
250:
172:
379:
Incompatible with higher temperature heat sources due to scaling issues during spray evaporation.
209:
35:
382:
Difficult to scale down to small sizes due to complexity and large numbers of parts required.
317:
204:
190:
510:
473:
219:
8:
350:
Does not need pre-treatment of sea water and tolerates variations in sea water conditions
231:
167:
514:
477:
328:
to reducing the pressure differentials if they are allowed to accumulate in the stages.
542:
214:
546:
534:
526:
439:
522:
518:
481:
429:
245:
238:
196:
178:
462:"Entropy Generation of Desalination Powered by Variable Temperature Waste Heat"
184:
559:
530:
443:
538:
275:
268:
162:
124:
363:
486:
461:
272:
434:
417:
24:
500:
366:
from power generation, industrial processes, or solar heating.
359:
24-hour-a-day continuous operation with minimum supervision
344:
Low energy consumption compared to other thermal processes
286:
459:
261:
Multiple-effect distillation or multi-effect distillation
362:
Can be adapted to any heat source, including hot water,
49:. Unsourced material may be challenged and removed.
455:
453:
557:
120:
450:
415:
16:Separation process used to purify sea water
485:
433:
324:70-75 °C, to avoid scale formation.
109:Learn how and when to remove this message
422:International Journal of Energy Research
369:Produce steadily high purity distillate.
285:
300:and the interior of the tubes in stage
281:
558:
353:Highly reliable and simple to operate
47:adding citations to reliable sources
18:
13:
14:
577:
503:Science of the Total Environment
373:
23:
523:10.1016/j.scitotenv.2019.07.351
34:needs additional citations for
494:
416:Panagopoulos, Argyris (2019).
409:
398:Multi-stage flash distillation
226:Multiple-effect humidification
143:Multi-stage flash distillation
58:"Multiple-effect distillation"
1:
403:
338:
307:
149:Multiple-effect distillation
7:
386:
10:
582:
393:Multiple-effect evaporator
251:Wave-powered desalination
173:Electrodialysis reversal
271:process often used for
222:–dehumidification (HDH)
210:Geothermal desalination
292:
318:operating temperature
289:
205:Freezing desalination
191:Membrane distillation
356:Low maintenance cost
282:Operating principles
220:Solar humidification
43:improve this article
515:2019ScTEn.693m3545P
478:2015Entrp..17.7530W
232:Seawater greenhouse
566:Water desalination
293:
215:Solar desalination
168:Membrane processes
125:Water desalination
487:10.3390/e17117530
472:(11): 7530–7566.
258:
257:
155:Vapor-compression
119:
118:
111:
93:
573:
551:
550:
498:
492:
491:
489:
457:
448:
447:
437:
413:
121:
114:
107:
103:
100:
94:
92:
51:
27:
19:
581:
580:
576:
575:
574:
572:
571:
570:
556:
555:
554:
499:
495:
458:
451:
435:10.1002/er.4948
414:
410:
406:
389:
376:
341:
310:
284:
246:water recycling
241:crystallization
239:Methane hydrate
197:Forward osmosis
179:Reverse osmosis
127:
115:
104:
98:
95:
52:
50:
40:
28:
17:
12:
11:
5:
579:
569:
568:
553:
552:
493:
449:
407:
405:
402:
401:
400:
395:
388:
385:
384:
383:
380:
375:
372:
371:
370:
367:
360:
357:
354:
351:
348:
345:
340:
337:
309:
306:
283:
280:
256:
255:
254:
253:
248:
242:
236:
235:
234:
229:
223:
212:
207:
202:
201:
200:
194:
188:
185:Nanofiltration
182:
176:
165:
160:
159:
158:
152:
146:
134:
133:
129:
128:
117:
116:
31:
29:
22:
15:
9:
6:
4:
3:
2:
578:
567:
564:
563:
561:
548:
544:
540:
536:
532:
528:
524:
520:
516:
512:
508:
504:
497:
488:
483:
479:
475:
471:
467:
463:
456:
454:
445:
441:
436:
431:
427:
423:
419:
412:
408:
399:
396:
394:
391:
390:
381:
378:
377:
374:Disadvantages
368:
365:
361:
358:
355:
352:
349:
346:
343:
342:
336:
332:
329:
325:
321:
319:
314:
305:
303:
299:
288:
279:
277:
274:
270:
266:
262:
252:
249:
247:
243:
240:
237:
233:
230:
227:
224:
221:
218:
217:
216:
213:
211:
208:
206:
203:
198:
195:
192:
189:
186:
183:
180:
177:
174:
171:
170:
169:
166:
164:
161:
156:
153:
150:
147:
144:
141:
140:
139:Distillation
138:
137:
136:
135:
131:
130:
126:
123:
122:
113:
110:
102:
91:
88:
84:
81:
77:
74:
70:
67:
63:
60: –
59:
55:
54:Find sources:
48:
44:
38:
37:
32:This article
30:
26:
21:
20:
506:
502:
496:
469:
465:
425:
421:
411:
333:
330:
326:
322:
315:
311:
301:
297:
294:
276:desalination
269:distillation
264:
260:
259:
163:Ion exchange
148:
105:
96:
86:
79:
72:
65:
53:
41:Please help
36:verification
33:
428:: 473–495.
244:High grade
509:: 133545.
404:References
364:waste heat
339:Advantages
308:Trade-offs
99:April 2017
69:newspapers
547:199387639
531:0048-9697
444:1099-114X
273:sea water
560:Category
539:31374511
387:See also
132:Methods
511:Bibcode
474:Bibcode
466:Entropy
267:) is a
83:scholar
545:
537:
529:
442:
85:
78:
71:
64:
56:
543:S2CID
228:(MEH)
175:(EDR)
151:(MED)
145:(MSF)
90:JSTOR
76:books
535:PMID
527:ISSN
440:ISSN
199:(FO)
193:(MD)
187:(NF)
181:(RO)
157:(VC)
62:news
519:doi
507:693
482:doi
430:doi
265:MED
45:by
562::
541:.
533:.
525:.
517:.
505:.
480:.
470:17
468:.
464:.
452:^
438:.
426:44
424:.
420:.
549:.
521::
513::
490:.
484::
476::
446:.
432::
302:n
298:n
263:(
112:)
106:(
101:)
97:(
87:·
80:·
73:·
66:·
39:.
Text is available under the Creative Commons Attribution-ShareAlike License. Additional terms may apply.