Flash distilasi (kadang-kadang disebut "keseimbangan distilasi") adalah teknik pemisahan satu tahap. Sebuah umpan campuran cairan dipompa melalui pemanas untuk menaikkan suhu dan entalpi campuran. ...Full description
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design of rope drum hoist for hydro power plant
design of rope drum hoist for hydro power plant
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Modul belajar Animasi flash berbahasa indonesia, dipersembahkan oleh SADANA Studio. Pengenalan, latihan, teori dan praktek, bahkan tips dan trik lengkap dibahas pada terbitan kedua ini. semoga berm...
Flash distillation notes
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EQUIPMENT DESIGN: BASIC CONCEPTS
GOALS: u D ef i ni ti ons and Con Con cepts u T ypes ypes of D esi gn u D esi gn M ethod th odol olog ogy y
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Equipment Design
EQUIPMENT CHARACTERIZATION
Input Streams
Operating Parameters 24/99
Output Streams
Size Parameters Equipment Design
DEFINITIONS EQUI PM ENT RATI NG: ð Gi ven the i nput str eams, oper ating par ameter s, and size parameter s, deter mine th e equipment per formance and output str eams
EQUI PM ENT SI ZI NG: ð Given the i nput str eams and the per formance specifi cati ons, esti mate the economi cally impor tant size parameter s usi ng approxi mate methods
EQUI PM ENT DESI GN: ð Produce a design in enough detail to gui de the fabr i cation of the item of equi pment 24/99
Equipment Design
Equipment Design Methodology
Set Performance Specifications
Determine Operational Constraints
Choose Equipment Type and Design Parameters
Try First
Perform Rating Calculations
N o I terate
Satisfy Specs & Constraints? Yes
Done
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Equipment Design
EXAMPLE #1: REFLUX DRUM ROBL EM : Design a r efl ux dr um for a di stil l ation col um F or a residence time of 15 minutes when half full, That has a length to diameter r atio L /D = 3.0, and I s hori zontal. PERATI NG CONDI TI ONS: F low r ate out of dr um i s 5,000 Kg/hr F l ow is 100% Ethanol (SG = 0.789)
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Equipment Design
REFLUX DRUM
From Overhead Condenser
D
Distillate
Reflux to Column
L
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Equipment Design
DESIGN CALCULATIONS
H oldup = (5000 kg/hr )(0.25 hr ) = 1250 kg 3 3 Densi ty = (0.789)(1000 kg/m ) = 789 kg/m 3 3 Vol ume = (2)(1250 kg)/(789 kg/m ) = 3.17 m
(To simplify the size cal culations, neglect the holdup in t dished heads of the drum.) 2 Vol ume = 3.1416 (D ) L
(but L = 3.0 D, so)
3 D = 3.17/(3)/(3.1416) So,
D = 0.695 m and L = 2.09 m. 24/99
Equipment Design
EXAMPLE #2: FLASH DRUM ROBL EM : Design a flash dr um that i To fl ash a str eam that is 60 mol % ethylene and 40 mol% water at a fl ow r ate of 800 kmol/hr , To produce a vapor that i s 99% ethylene At a fr acti onal r ecover y of ethylene of 99 % The flash drum i s a ver ti cal pr essur e with an L /D = 4.0. PERATI NG CONSTRAI NTS: L ow entr ai nment of water i n the vapor 10 mi nu te holdup of l iqui d when dr um is 1/2 ful l 24/99
Equipment Design
FLASH DRUM VAPOR
FEED
Heating or Cooling
LIQUID
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Equipment Design
DESIGN PROCEDURE BA SI C DE SI GN VARI ABL ES: Pressur e P and H eat Duty Q.. Guess val ues for P and Q. Do the adiabati c flash calculation to deter mi ne V, L and their compositi ons an temperature I f the per f ormance specifi cati ons are satisf ied, proceed to size the drum. I f not iter ate on P and Q. Size drum to satisfy entr ainment, li qui d holdup and L / constraints.
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Equipment Design
SUMMARY F or ver y simple situations, the design calculations are explicit. F or most situations, the design calcul ations involve a tr i al-and-er r or search for those val ues of key design var iables that satisfy the per f ormance specificati ons and constraints. The detail s of the design methodology wil l dif fer fr om one equi pment type to another . The details of the desi gn methodology may al so differ for dif fer ent per formance specif icati ons for the same typ of equi pment. 24/99