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7/24/2019 Intercambiadores de Liquido a Liquido
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INTERCAMBIADORES DE LIQUIDO A LIQUIDO.
1.1.DISEO MECANICO.
Se presentah aqu los principales aspectos a tener en cuenta para el
diseo mecnico y estructural de los intercambiadores de tubo y
coraza.
1.1.1. Esfuerzos en tubos.
En este apartado se realiza un anlisis de los principales esfuerzos que pueden
presentarse en intercambiadores de calor. Se ha tomado como ejemplo un
intercambiador de tubo y coraza.
Para el diseo y clculo de los tubos y la coraza se utilizan bsicamente los
cdigos E!" y "S!E seccin #$$$ di%isin &.
1.1.2. Esfuerzos en coraza.
1.1.3. Esfuerzos en cabezales.
'os esfuerzos en los cabezales corresponden principalmente a los
esfuerzos longitudinales descritos en el prrafo anterior. Se presentan
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las principales clases de tapas cabezales utilizados en este tipo de
equipos. (tomado de ).
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Sujecin tapas planas.
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Figura . clases de uniones entre las tapas y la coraza.
Discontinuidad en esfuerzos tapas semiesfricas.
Figura refuerzo de penetraciones en la lmina.
!enetracin en la lmina.
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Figura "todos para soportar recipientes a presin. #fraas $.
"an%oles. Soportes recipientes.
Figura &ipos de uniones con brida.
'niones con flanges o bridas.
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Figura "anifold.
"anifold
Esfuerzos trmicos. tubos bifurcados.
Figura Esfuerzos trmicos.
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Figura !andeo de tubos debido a diferente e(pansin entre las lminas del
cabezal.
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Figura
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Figura "(imo esfuerzo de corte en la camisa en funcin de la posicin a(ial.
1.1.). Esfuerzos en espejos. !*&+,- ES!E, #/E*DE+ S/EE&$.
*igura Patrn de distribucin de los tubos en los espejos.
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*igura Ensamble de los tubos en el espejo.
*igura Espejos.
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+eat E,changers - esign Speci/cations
EXPERT ENGINEERS AND DRAFTSMEN WITH ON-SITE MANUFACTURING.
Shell & Tube Heat Exchangers are the most common type of heat exchanger usedin the chemical process industry. As its name implies, this type of heat exchanger
consists of a shell filled with a bundle of tubes and sealed at each end by a
tubesheet isolating the tubes and the shell.
A fluid or gas flows through the tubes while another fluid or gas flows through
the shell causing heat to transfer through the tube walls. The set of tubes is
called a tube bundle and may be composed of various tube configurations plain,
longitudinally finned, etc.
Shell & Tube Heat Exchangers are used in applications where the demands from
high temperatures and pressures are significant.
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!endel designs and fabricates all three types of Shell & Tube Heat Exchangers
"ixed Tubesheet, #$tube and "loating Tubesheet.
"igura intercambiador con espe%os flotantes.
The Fixed Tubesheetdesign consists of two stationary tubesheets attached to
the shell. The bundle of straight tubes are connected between the tubesheets
and contain baffles to direct the flow around the tubes in order to generate thereuired heat transfer. A head assembly is attached to each tubesheet.
The U-tubedesign consists of straight length tubes bent into a #$shape with
both ends terminating at the tubesheet. The tube bundle is fitted with supports
or flow baffles. The tubesheet'tube bundle is placed in the shell and bolted
between the head flange and body flange. A head assembly is reuired to direct
the fluid into and out of the tube bundle. This configuration allows for the entire
tube bundle to be removable.
A Floating Tubesheetdesign is similar to the "ixed Tubesheet design except
one tubesheet is allowed to move axially within the shell while the other
tubesheet is
fixed. This configuration also allows for the tube bundle to be removable.
!endel is here to serve you and provide the highest uality custom built Shell &
Tube Heat Exchangers to meet your application reuirements. (e welcome the
opportunity topro%ide you a quote.
)lease see ourcontact pageto submit your reuest.
http://www.bendelcorp.com/contact_quoterequest.htmlhttp://www.bendelcorp.com/contact_main.htmlhttp://www.bendelcorp.com/contact_main.htmlhttp://www.bendelcorp.com/contact_quoterequest.html7/24/2019 Intercambiadores de Liquido a Liquido
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Figura Dimensiones caractersticas en un espejo.
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Figura
Figura
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*igura . +erramienta para e,pansin de tubos.
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1.1.0. Esfuerzos en deflectores.1.1.. ouillas.1.1.4. "an%oles y %and%oles.1.1.5. Soportes.
1.2. Soft6are para dise7o de intercambiadores de tubo y coraza.
E,istehn numerosos programas que se pueden utilizar para el clculo y
diseo de este tipo de intercambiadores. $ncluso una solucin simple es
desarrollar su propa hoja de clculo para realizar los principales clculos.
"lgunos programas incluyen el diselo t0rmico e hidrulico1 asi como el
diseo mecnico de acuerdo con los estandarees utilizados ("S!E1 E!"1
"P$).
Entre los programas mencionamos los siguientes2
8amfle(. 9&S s%ell and tube %eat e(c%anger design.
:odecalc # dise7o mecnico$
&%is pac;age contains 2 different soft6areas;eted !late /eat E(c%anger Design #!%e($ soft6are Demo
?ersion
2= ?isualasic!o6er!ac;sSetup from "icrosoft 6ebsite
&%e !%ysical properties soft6are is a separate soft6are and can be
do6nloaded separately form
6ebbusterz.com or 6ebbusterz.net
-ormally t%e p%ysical properties are generated separately and sa@ed toa file. &%e soft6are
t%en lin;s to t%e p%ysical properties soft6are and %as a feature to import
t%e p%ysical properties file.
A-S&+':&A,-S B
A-S&*CC &/E S,F&9*+E A- &/E ,+DE+ SE& *,?E
&o install please clic; on t%e setup.e(e file under t%e soft6are folder. &%e
installer 6ill attempt to
@erify if you %a@e t%e correct system files to run t%is soft6are. At 6ill also
attempt to install any missing
system files or frame6or; before installing t%e soft6are.
Af t%e installation fails t%en ma;e sure t%at "icrosoft .-et frame6or; 3.0
are installed on your computer
before re=installation. "ost ne6 computers 6ill %a@e t%is reuirements.
Af you dont %a@e t%is reuirement< t%ere is t6o 6ays of installing
"icrosoft .-et frame6or; 3.0
a$ +un 6indo6s update
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,+
b$ Do6nload t%is files from "icrosoft 6ebsite #"icrosoft .-et frame6or;
3.0 AS F+EE you dont need to pay for it$
%ttpGHH666.microsoft.comHdo6nloadHenHdetails.asp(IidJ21
/E*&=C?=ye%=)K)
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1.2.1. 8amfle(.
Esta desarrollado sobre una hoja de clculo de e,cell.Es de licencia libre
pero tiene un n3mero limitado de corridas.
1.2.2. 9&S.1.2.3. :odecalc.
1.3.Ejemplo integral de clculo.
" contiunuacin se presenta un ejercicio tomado de t0sis diseo de
intercambiadores1 en el cual s erealiza un diseo completo del
intercambiador1 aplicando los conceptos estudiados a lo largo de este
captulo.
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How to Design a Shell-and-Tube Heat Exchanger
R. Shankar Subramanian
A lot has been written about designing heat exchangers, and specifically, shell-and-tubeheat exchangers. For example, the book by Kern (1 published in 1!"# details basic designprocedures for a $ariety of heat exchangers. %ince the publication of that book, with the
ad$ent of computers, design procedures ha$e become sophisticated e$en though the basicgoals of design remain the same. &ecause it is possible to specify an infinite number ofdifferent heat exchangers that would perform the gi$en ser$ice (heat load, we ha$e toidentify the specific heat exchanger that would do it sub'ect to certain constraints. heseconstraints can be based on allowable pressure drop considerations either on the shell-sideor on the tube-side or both, and usually include that of minimi)ing the o$erall cost. Anarticle in 1!*! by aborek (+ outlines how heat exchanger design techniues e$ol$ed o$erthe years since the appearance of the book by Kern. ore recent de$elopments arediscussed in numerous articles in the maga)ine /hemical 0ngineering.2ere is a step-by-step approach to specifying a new shell-and-tube heat exchanger. 3e shallfocus on sensible heat transfer, and make extensi$e use of /hapter 11 in 4erry5s 2andbook(6. From hereon, references to page numbers, table numbers, and euation numbers arefrom 4erry5s 2andbook.7sually, the flow rates and the physical properties of the two streams in$ol$ed arespecified, and the temperatures at which the fluids are a$ailable are known. 8f the outgoingtemperature of one of the streams is not specified, usually a constraint (e.g. the temperatureof the cooling water cannot exceed !! is gi$en. hen, by an energy balance, the outgoingtemperature of the second stream can be calculated along with the heat duty. C4LSize
1. he heat duty Q is usually fixed by the reuired ser$ice. he selected heat exchanger hasto meet or exceed this reuirement.+. ake an approximate estimate of the si)e of the heat exchanger by using a reasonableguess for the o$erall heat transfer coefficient. For typical shell-and-tube heat exchangers ina chemical process or a refinery, ables 11-6 and 11-9 can be used as a starting point for theestimate. 7sing this estimate, calculate the heat transfer area . his will gi$e you an idea ofthe approximate si)e of the heat exchanger, and therefore its cost. &ased on the cost, adetermination is made on how much time is worth in$esting in a detailed design.A6. %elect the stream that should be placed on the tube side. he tube side is used for thefluid that is more likely to foul the walls, more toxic or more corrosi$e, or for the fluid withthe higher pressure. /leaning of the inside of the tubes is easier than cleaning the outside.3hen a gas or $apor is used as a heat exchange fluid, it is typically introduced on the shellside. Also, high1
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$iscosity liuids, for which the pressure drop for flow through the tubes might beprohibiti$ely large, can be introduced on the shell side.9. he next step is to determine the approximate number of tubes needed to do the 'ob.&ecause we ha$e an idea of the approximate heat transfer area, we can write tN(toANDL:;
where is the , 1#, 1+, 1?, or +# feet. @ikewise, the
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?. Dou need to estimate the number of baffles to be used and the spacing among them. Doucan read about baffles from pages 11-9+ and 11-96. Gormally, baffles are eually spaced.he minimum baffle spacing is one-fifth of the shell diameter, but not less than + inches,and the maximum is determined by considerations in$ol$ing supporting the tube bundle. Asimple formula from 4erry for estimating the maximum is inches, where is the .