Docsity
Docsity

Prepare for your exams
Prepare for your exams

Study with the several resources on Docsity


Earn points to download
Earn points to download

Earn points by helping other students or get them with a premium plan


Guidelines and tips
Guidelines and tips

IDEAL PLUG FLOW REACTOR, Study Guides, Projects, Research of Design

In an ideal PFR, is the absolute residence time for mass flowing through the reactor, not the average residence time as in a CSTR. 3. Compare ideal batch and ...

Typology: Study Guides, Projects, Research

2021/2022

Uploaded on 09/27/2022

manager33
manager33 🇬🇧

4.4

(33)

23 documents

1 / 6

Toggle sidebar

Related documents


Partial preview of the text

Download IDEAL PLUG FLOW REACTOR and more Study Guides, Projects, Research Design in PDF only on Docsity! 1 IDEAL PLUG FLOW REACTOR Characteristics of ideal plug flow PERFECT MIXING IN THE RADIAL DIMENSION (UNIFORM CROSS SECTION CONCENTRATION) NO MIXING IN THE AXIAL DIRECTION, OR NO AXIAL DISPERSION (SEGREGATED FLOW) TRACER PULSE INPUT AT t = 0 TRANSLATED TO EQUAL PULSE OUTPUT AT t = = L/v (L = PFR length, v = average velocity) COMPARE WITH CSTR RESPONSE TO TRACER PULSE DISPERSION 0 Q CO Q CL L 0 time 0 time 2 In an ideal PFR, concentration is a function of both distance along the flow path, x, and time, t: C = C(x,t) For a mass balance on a reacting compound, take mass balance on differential axial element with uniform reaction potential (concentration), where dV = differential volume A = cross sectional area dx = differential distance and dV = Adx Mass balance over differential element on a reactant, C In = QCx Out = QCx+dx Generation = dVrC = AdxrC Accumulation = dV Cx t Adx Cx t QCx – QCx+dx + dVrC = dV Cx t Cx+dx = Cx + dCx Q(Cx – Cx – dCx) + dVrC = dV Cx t Q Cx V rC Cx t Cx V Q rC since Q is constant Q Cx Q Cx+dx x x+dx A 5 Where Q = 0.25 m 3 /s A = channel cross section between baffles = 18 m 2 rd = rate of microorganism kill in presence of chlorine = -kdX X = concentration of microorganisms at any point in contact reactor Xo = influent concentration of microorganisms = 10 6 E. coli/100 ml kd = 5 hr -1 rc = rate of chlorine decay (from microorganism Cl-demand) = -kcX kc = 10 -5 (mg-chlorine/L)(#/100mL) -1 hr -1 2 rate expressions, 2 constituents, 2 coupled mass balances find: 1. reactor volume and flow path length, L, such that XL < 10 3 cells/100 ml 2. chlorine concentration which must be added to insure that there is detectable chlorine at PFR exit (detection level = CL = 0.05 mg/L) 1. Steady-state mass balance on cells XL = Xoexp(-kd ) = (1/kd)ln(Xo/XL) = (1/5)(hr)ln(10 6 /10 3 ) = 1.4 hr V = Q = 0.25 m 3 /s*3600 s/hr*1.4 hr = 1,260 m 3 L = V/A = 1,260 m 3 /18 m 2 = 70 m 3. Steady state mass balance on chlorine 6 dCc d k cX k cXo exp( k dd ) dCc Cco CL k cXo exp( kd )d 0 CL Cco (k cXo) k d k cXo exp( kd ) kd CL Cco (k cXo) k d (1 exp( kd )) CCO = 0.05 + (10 -5 (10 6 )/5)(1-exp(-5(1.4)) = 2.05 mg/L Chlorine contact PFR 1.0E+02 1.0E+03 1.0E+04 1.0E+05 1.0E+06 0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 = x/v (hr) E . c o li ( # / 1 0 0 m L ) 0.00 1.00 2.00 3.00 4.00 C c ( m g - c h lo r in e / L ) X Cc
Docsity logo



Copyright © 2024 Ladybird Srl - Via Leonardo da Vinci 16, 10126, Torino, Italy - VAT 10816460017 - All rights reserved