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Continuous stirred-tank reactor

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3210: 1416: 1332:, or exit age distribution. Not all fluid particles will spend the same amount of time within the reactor. The exit age distribution (E(t)) defines the probability that a given fluid particle will spend time t in the reactor. Similarly, the cumulative age distribution (F(t)) gives the probability that a given fluid particle has an exit age less than time t. One of the key takeaways from the exit age distribution is that a very small number of fluid particles will never exit the CSTR. Depending on the application of the reactor, this may either be an asset or a drawback. 4926: 1374:. The presence of corners or baffles in a reactor often results in some dead space where the fluid is poorly mixed. Similarly, a jet of fluid in the reactor can cause short-circuiting, in which a portion of the flow exits the reactor much quicker than the bulk fluid. If dead space or short-circuiting occur in a CSTR, the relevant chemical or biological reactions may not finish before the fluid exits the reactor. Any deviation from ideal flow will result in a residence time distribution different from the ideal distribution, as seen at right. 5556: 1400: 6055: 106: 1345: 6067: 1321: 93:. In a perfectly mixed reactor, reagent is instantaneously and uniformly mixed throughout the reactor upon entry. Consequently, the output composition is identical to composition of the material inside the reactor, which is a function of residence time and reaction rate. The CSTR is the ideal limit of complete mixing in reactor design, which is the complete opposite of a 4922:
PFRs, which may be a challenge in applications where space is limited. However, one of the added benefits of dilution in CSTRs is the ability to neutralize shocks to the system. As opposed to PFRs, the performance of CSTRs is less susceptible to changes in the influent composition, which makes it ideal for a variety of industrial applications:
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must be taken into account. As seen above, an increase in the number of CSTRs in series will decrease the total reactor volume. Since cost scales with volume, capital costs are lowered by increasing the number of CSTRs. The largest decrease in cost, and therefore volume, occurs between a single CSTR
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To model systems that do not obey the assumptions of constant temperature and a single reaction, additional dependent variables must be considered. If the system is considered to be in unsteady-state, a differential equation or a system of coupled differential equations must be solved. Deviations of
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CSTRs facilitate rapid dilution of reagents through mixing. Therefore, for non-zero-order reactions, the low concentration of reagent in the reactor means a CSTR will be less efficient at removing the reagent compared to a PFR with the same residence time. Therefore, CSTRs are typically larger than
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in the reactor and the rate constant. A key assumption when modeling a CSTR is that any reactant in the fluid is perfectly (i.e. uniformly) mixed in the reactor, implying that the concentration within the reactor is the same in the outlet stream. The rate constant can be determined using a known
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is the molar flow rate of the feed. When the same process is applied to a cascade of CSTRs as seen in the graph with three CSTRs, the volume of each reactor is calculated from each inlet and outlet fractional conversion, therefore resulting in a decrease in total reactor volume. Optimum size is
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While the ideal CSTR model is useful for predicting the fate of constituents during a chemical or biological process, CSTRs rarely exhibit ideal behavior in reality. More commonly, the reactor hydraulics do not behave ideally or the system conditions do not obey the initial assumptions. Perfect
31: 3336:. Therefore the total reactor volume is independent of the number of CSTRs for a zeroth order reaction. Therefore, cost is not a function of the number of reactors for a zeroth order reaction and does not decrease as the number of CSTRs increases. 3230:
and controls, construction, installation, and maintenance that accompany larger cascades. Therefore as the number of CSTRs increases, the operating cost increases. Therefore, there is a minimum cost associated with a cascade of CSTRs.
2514: 1387:(PFRs) either in series or in parallel. For examples, an infinite series of ideal CSTRs is hydraulically equivalent to an ideal PFR. Reactor models combining a number of CSTRs in series are often termed tanks-in-series (TIS) models. 4511: 82:. A CSTR often refers to a model used to estimate the key unit operation variables when using a continuous agitated-tank reactor to reach a specified output. The mathematical model works for all fluids: liquids, gases, and 3128: 1299: 2779: 3837: 1382:
Although ideal flow reactors are seldom found in practice, they are useful tools for modeling non-ideal flow reactors. Any flow regime can be achieved by modeling a reactor as a combination of ideal CSTRs and
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mixing is a theoretical concept that is not achievable in practice. For engineering purposes, however, if the residence time is 5–10 times the mixing time, the perfect mixing assumption generally holds true.
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Non-ideal hydraulic behavior is commonly classified by either dead space or short-circuiting. These phenomena occur when some fluid spends less time in the reactor than the theoretical residence time,
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When the volumes of the individual CSTRs in series vary, the order of the CSTRs does not change the overall conversion for a first order reaction as long as the CSTRs are run at the same temperature.
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the CSTR behavior can be considered by the dispersion model. CSTRs are known to be one of the systems which exhibit complex behavior such as steady-state multiplicity, limit cycles, and chaos.
3307: 2036: 1972: 1871: 1205: 3629: 3546: 2372: 751: 4815: 2852: 658: 5086:. Tchobanoglous, George,, Stensel, H. David,, Tsuchihashi, Ryujiro,, Burton, Franklin L. (Franklin Louis), 1927-, Abu-Orf, Mohammad,, Bowden, Gregory (Fifth ed.). New York, NY. 1138: 3992: 3958: 980: 1462: 3409: 3381: 4355: 4310: 3719: 3674: 6040: 4731: 4691: 4591: 4551: 3877: 3334: 1030:, is always equal to the reactor volume divided by the fluid flow rate. See the next section for a more in-depth discussion on the residence time distribution of a CSTR. 2810: 5386:
Hurtado, F.J.; Kaiser, A.S.; Zamora, B. (March 2015). "Fluid dynamic analysis of a continuous stirred tank reactor for technical optimization of wastewater digestion".
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for an ideal CSTR. The values of the outlet concentration and residence time are major design criteria in the design of CSTRs for industrial applications.
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with two CSTRs, equal volumes should be used. As the number of ideal CSTRs (n) approaches infinity, the total reactor volume approaches that of an ideal
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Cost initially decreases with the number of CSTRs as volume decreases but as operational costs increase, the total cost eventually begins to increase.
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Equation 6 can be solved by integration after substituting the proper rate expression. The table below summarizes the outlet concentration of species
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is the total amount of time a discrete quantity of reagent spends inside the reactor. For an ideal reactor, the theoretical residence time,
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achieved when the area above the rectangles from the CSTRs in series that was previously covered by a single CSTR is maximized. For a
1584: 5545: 4930: 5512: 3143: 2213: 97:(PFR). In practice, no reactors behave ideally but instead fall somewhere in between the mixing limits of an ideal CSTR and PFR. 846: 5721: 143: 5446: 5370: 5293: 5143: 5091: 2122: 2043: 224:(valid for most liquids; valid for gases only if there is no net change in the number of moles or drastic temperature change) 767: 4159: 4051: 1514: 138: 3246: 1977: 1913: 1812: 1149: 5345: 5049: 2305: 3551: 3468: 6030: 679: 6071: 6035: 3345: 2815: 592: 4786: 5879: 5646: 5317:
Stokes, R. L.; Nauman, E. Bruce (1970). "Residence Time Distribution Functions for Stirred Tanks in Series".
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and having two CSTRs in series. When considering operating cost, operating cost scales with the number of
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Exit age distribution E(t) and cumulative age distribution F(t) functions for a CSTR with dead space
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Cascades of CSTRs, also known as a series of CSTRs, are used to decrease the volume of a system.
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An ideal CSTR will exhibit well-defined flow behavior that can be characterized by the reactor's
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The behavior of a CSTR is often approximated or modeled by that of an ideal CSTR, which assumes
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When the cascade of CSTRs is isothermal with identical reactors, the concentration is given by
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and B is the desired product, the cascade of CSTRs is favored with a fresh secondary feed of
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Monsen, Nancy E.; Cloern, James E.; Lucas, Lisa V.; Monismith, Stephen G. (September 2002).
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Exit age distribution E(t) and cumulative age distribution F(t) functions for an ideal CSTR
1012: 929: 331: 75: 2509:{\displaystyle C_{Ai}={\frac {-1+{\sqrt {1+4k_{i}\tau _{i}C_{A(i-1)}}}}{2k_{i}\tau _{i}}}} 2382: 8: 5874: 5857: 5837: 5817: 5232:"A comment on the use of flushing time, residence time, and age as transport time scales" 1496: 1053:. Generally, as the temperature increases so does the rate at which the reaction occurs. 5399: 5247: 5198: 4925: 2207: 5884: 5630: 5261: 5161: 5109: 4962: 4955: 1800: 1423:
As seen in the graph with one CSTR, where the inverse rate is plotted as a function of
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From a rearrangement of the equation given for identical isothermal CSTRs running a
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first order, constant density reaction in a cascade of identical CSTRs operating at
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From this, the cumulative residence time distribution (F(t)) can be calculated as
5772: 5767: 5757: 5407: 4506:{\displaystyle {\frac {d}{d}}={\frac {k_{1}}{k_{2}}}^{n_{1}-n_{2}}^{m_{1}-m_{2}}} 2527:
can be calculated. At the concentration at the jth reactor in series is given by
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Introduction to Chemical Engineering Kinetics and Reactor Design, Second Edition
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As the number of CSTRs in series increases, the total reactor volume decreases.
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and B is the desired product, a cascade of CSTRs with a high concentration of
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and B is the desired product, a cascade of CSTRs with an inlet stream of high
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but CSTRs in general are typically not chosen when the desired product is
5984: 5974: 5969: 4267:, respectively, we can obtain a relationship between the two by dividing 3631:, respectively, we can obtain a relationship between the two by dividing 3123:{\displaystyle F(t)={\frac {C_{n}}{C_{o}}}=1-e^{-{\frac {nt}{\bar {t}}}}} 1399: 5555: 5911: 5864: 5787: 5696: 263: 5136:
Water quality engineering : physical/chemical treatment processes
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at steady state in a cascade of CSTRs, the general design equation is
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A continuous fluid flow containing non-conservative chemical reactant
1294:{\displaystyle C_{A}={\frac {-1+{\sqrt {1+4k\tau C_{Ao}}}}{2k\tau }}} 2774:{\displaystyle {\frac {C_{j}}{C_{o}}}=1-e^{-{\frac {nt}{\bar {t}}}}} 6014: 5916: 3832:{\displaystyle {\frac {d}{d}}={\frac {k_{1}}{k_{2}}}^{n_{1}-n_{2}}} 3133: 1049:
empirical reaction rate that is adjusted for temperature using the
1034: 227: 5288:. Davis, Robert J. (International ed.). Boston: McGraw-Hill. 1344: 521:{\displaystyle 2.{\frac {dN_{A}}{dt}}=F_{Ao}-F_{A}+V\nu _{A}r_{A}} 105: 5954: 5847: 5625: 5620: 221: 5490: 5441:(second ed.). Boca Raton, FL, USA: CRC Press. p. 181. 5999: 5591: 4984: 83: 1669:{\displaystyle \tau _{i}={\frac {C_{A(i-1)}-C_{Ai}}{-r_{Ai}}}} 34:
Diagram showing the setup of a continuous stirred-tank reactor
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List of largest biomedical companies by market capitalization
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Wastewater engineering : treatment and resource recovery
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For a parallel reaction with two or more reactants such as
3227: 3194:{\displaystyle \sigma _{t}^{2}={\frac {{\bar {t}}^{2}}{n}}} 2293:{\displaystyle C_{Am}=C_{Ao}-\sum _{i=1}^{m}k_{i}\tau _{i}} 5229: 914:{\displaystyle 6.\ r_{A}={\frac {1}{\tau }}(C_{Ao}-C_{A})} 5605: 5601: 5340:. Hoboken, new Jersey: Wiley. pp. 241–253, 349–358. 4952:
Lagoon treatment systems for natural wastewater treatment
1581:, we can determine that for a single CSTR in series that 1044:, is generally dependent on the concentration of species 2206:
At steady state, the general equation for an isothermal
197:{\displaystyle {\Bigl (}{\frac {dN_{A}}{dt}}=0{\Bigr )}} 2189:{\displaystyle C_{Am}={\frac {C_{Ao}}{(1+k\tau )^{m}}}} 2110:{\displaystyle C_{A2}={\frac {C_{Ao}}{(1+k\tau )^{2}}}} 666:
can then be rewritten in terms of the concentration of
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As n → ∞, F(t) approaches the ideal PFR response. The
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is the average residence time of the cascade given by
961: 835:{\displaystyle 5.\ r_{A}={\frac {Q}{V}}(C_{Ao}-C_{A})} 4889: 4867: 4845: 4823: 4789: 4761: 4739: 4699: 4659: 4629: 4599: 4559: 4519: 4363: 4318: 4273: 4162: 4149:{\displaystyle {\frac {d}{dt}}=k_{1}^{n_{1}}^{m_{1}}} 4054: 4027: 4000: 3966: 3932: 3907: 3885: 3845: 3727: 3682: 3637: 3554: 3471: 3444: 3417: 3389: 3361: 3315: 3249: 3146: 2869: 2818: 2789: 2535: 2391: 2308: 2216: 2125: 2046: 1980: 1916: 1907:
is the outlet concentration of A from the first CSTR
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where n is the total number of CSTRs in series, and
1574:{\displaystyle \tau ={\frac {C_{Ao}-C_{A}}{-r_{A}}}} 5385: 3348:, utilizing a cascade of CSTRs can achieve greater 3309:, the volume of each individual CSTR will scale by 2040:Plugging in the first CSTR equation to the second: 5081: 4897: 4875: 4853: 4831: 4809: 4769: 4747: 4725: 4685: 4645: 4615: 4585: 4545: 4505: 4349: 4304: 4259: 4148: 4040: 4013: 3986: 3952: 3915: 3893: 3871: 3831: 3713: 3668: 3623: 3540: 3457: 3430: 3403: 3375: 3328: 3301: 3193: 3122: 2846: 2804: 2773: 2508: 2366: 2292: 2188: 2109: 2030: 1966: 1899: 1865: 1779: 1749: 1722: 1688: 1668: 1573: 1486: 1456: 1365: 1293: 1199: 1132: 1021: 974: 938: 913: 834: 745: 652: 520: 417: 196: 5133: 3302:{\displaystyle \tau ={\frac {C_{Ao}-C_{Am}}{mk}}} 2031:{\displaystyle C_{A2}={\frac {C_{A1}}{1+k\tau }}} 1967:{\displaystyle C_{A1}={\frac {C_{Ao}}{1+k\tau }}} 1866:{\displaystyle C_{A1}={\frac {C_{Ao}}{1+k\tau }}} 1503:for the same reaction and fractional conversion. 189: 149: 6085: 3217:When determining the cost of a series of CSTRs, 1511:From the design equation of a single CSTR where 1200:{\displaystyle C_{A}={\frac {C_{Ao}}{1+k\tau }}} 1001:is the reactor/outlet concentration of species A 5283: 4974:Loop reactor for production of pharmaceuticals 1315: 291:is converted to products via chemical reaction 5506: 5466:"Visual Encyclopedia of Chemical Engineering" 5437:Kadlec, Robert H.; Wallace, Scott D. (2009). 5436: 5286:Fundamentals of chemical reaction engineering 4958:for the stabilization of wastewater biosolids 3624:{\displaystyle {\frac {d}{dt}}=k_{2}^{n_{2}}} 3541:{\displaystyle {\frac {d}{dt}}=k_{1}^{n_{1}}} 2518: 2367:{\displaystyle C_{Am}=C_{Ao}-mk_{i}\tau _{i}} 755:Equation 4 can then be rearranged to isolate 580:Applying the assumptions of steady state and 5336:Hill, Charles G.; Root, Thatcher W. (2014). 5316: 5181:Bolin, Bert; Rodhe, Henning (January 1973). 4937: 4755:in the feed and small secondary streams of 2119:Therefore for m identical CSTRs in series: 746:{\displaystyle 4.\ 0=QC_{Ao}-QC_{A}-Vr_{A}} 5513: 5499: 5363:Chemical Reaction Engineering, 3rd Edition 5360: 5180: 5166:: CS1 maint: location missing publisher ( 5138:. Lawler, Desmond F. Hoboken, New Jersey. 5114:: CS1 maint: location missing publisher ( 5035: 5033: 3901:in order to maximize the concentration of 1377: 5255: 5206: 4810:{\displaystyle {\ce {A -> B -> C}}} 3234: 2847:{\displaystyle {\bar {t}}={\frac {V}{Q}}} 1506: 653:{\displaystyle 3.\ 0=F_{Ao}-F_{A}-Vr_{A}} 552:is the molar flow rate outlet of species 313:Integral mass balance on number of moles 5546:Competitions and prizes in biotechnology 5335: 5319:Canadian Journal of Chemical Engineering 4931:Newtown Creek Wastewater Treatment Plant 4924: 4883:as the back mixing from the CSTR favors 3208: 1464:where V is the total reactor volume and 1414: 1398: 1343: 1319: 540:is the molar flow rate inlet of species 104: 29: 5039: 5030: 4968: 1133:{\displaystyle C_{A}={C_{Ao}}-{k\tau }} 1064:Outlet Concentration for an Ideal CSTR 992:is the inlet concentration of species A 14: 6086: 5077: 5075: 5073: 5071: 5069: 5067: 5065: 5063: 5061: 4961:Treatment wetlands for wastewater and 1757:is the outlet concentration of A, and 5494: 5460: 5458: 5129: 5127: 5125: 5044:. New York: Oxford University Press. 5042:The Engineering of Chemical Reactions 3987:{\displaystyle {\ce {A + D -> C}}} 3953:{\displaystyle {\ce {A + D -> B}}} 2210:at in a cascade of CSTRs is given by 975:{\displaystyle \tau ={\tfrac {V}{Q}}} 266:conditions, or constant temperature ( 6066: 5279: 5277: 5275: 1410: 1394: 64:continuous-flow stirred-tank reactor 5058: 1457:{\displaystyle {\frac {V}{F_{Ao}}}} 946:is the theoretical residence time ( 24: 5455: 5122: 1427:, the area in the box is equal to 211:is the number of moles of species 25: 6105: 5520: 5272: 5082:Metcalf & Eddy (2013-09-03). 3404:{\displaystyle {\ce {A -> C}}} 3376:{\displaystyle {\ce {A -> B}}} 3340:Selectivity of parallel reactions 3240: 1335: 109:Cross-sectional diagram of a CSTR 6065: 6054: 6053: 5554: 5470:encyclopedia.che.engin.umich.edu 5134:Benjamin, Mark M. (2013-06-13). 1730:is the feed concentration of A, 1051:Arrhenius temperature dependence 662:The molar flow rates of species 587:= −1, Equation 2 simplifies to: 252:is the concentration of species 6031:Index of biotechnology articles 5430: 5379: 4916: 4913:is chosen for these reactions. 4350:{\displaystyle {\frac {d}{dt}}} 4305:{\displaystyle {\frac {d}{dt}}} 3714:{\displaystyle {\frac {d}{dt}}} 3669:{\displaystyle {\frac {d}{dt}}} 2376: 2201: 245:is the reaction rate constant, 122:enters an ideal CSTR of volume 40:continuous stirred-tank reactor 18:Continuous stirred tank reactor 6036:List of biotechnology articles 5354: 5329: 5310: 5223: 5174: 4817:also have selectivity between 4800: 4794: 4726:{\displaystyle m_{1}<m_{2}} 4686:{\displaystyle n_{1}>n_{2}} 4653:is favored. In the case where 4638: 4632: 4608: 4602: 4586:{\displaystyle m_{1}>m_{2}} 4546:{\displaystyle n_{1}>n_{2}} 4474: 4465: 4436: 4427: 4394: 4386: 4378: 4370: 4333: 4325: 4288: 4280: 4238: 4229: 4213: 4204: 4177: 4169: 4130: 4121: 4105: 4096: 4069: 4061: 3977: 3943: 3872:{\displaystyle n_{1}>n_{2}} 3800: 3791: 3758: 3750: 3742: 3734: 3697: 3689: 3652: 3644: 3605: 3596: 3569: 3561: 3522: 3513: 3486: 3478: 3394: 3366: 3355:For a given parallel reaction 3329:{\displaystyle {\frac {1}{m}}} 3174: 3117: 3102: 3094: 3076: 3067: 3055: 3025: 3017: 2999: 2974: 2950: 2941: 2879: 2873: 2825: 2796: 2768: 2753: 2745: 2727: 2718: 2706: 2676: 2668: 2650: 2625: 2601: 2592: 2471: 2459: 2174: 2158: 2095: 2079: 1794: 1624: 1612: 908: 879: 829: 800: 412: 398: 392: 378: 372: 358: 352: 338: 13: 1: 5880:Genetically modified organism 5647:Biotechnology industrial park 5023: 100: 5408:10.1016/j.watres.2014.11.053 2525:residence time distributions 260:is the order of the reaction 7: 5870:Environmental biotechnology 5361:Levenspiel, Octave (1998). 5008:Oscillatory baffled reactor 4991: 3140:into a cascade of CSTRs is 3136:associated with F(t) for a 1330:residence time distribution 1316:Residence time distribution 1308:Numerical solution required 113: 70:), is a common model for a 10: 6110: 5236:Limnology and Oceanography 5208:10.3402/tellusa.v25i1.9644 5040:Schmidt, Lanny D. (1998). 2805:{\displaystyle {\bar {t}}} 2519:Non-ideal cascade of CSTRs 566:stoichiometric coefficient 6049: 6023: 5930: 5810: 5740: 5689: 5680: 5639: 5584: 5563: 5552: 5541:Timeline of biotechnology 5528: 5257:10.4319/lo.2002.47.5.1545 4938:Environmental engineering 4898:{\displaystyle {\ce {C}}} 4876:{\displaystyle {\ce {B}}} 4854:{\displaystyle {\ce {C}}} 4832:{\displaystyle {\ce {B}}} 4770:{\displaystyle {\ce {D}}} 4748:{\displaystyle {\ce {A}}} 3916:{\displaystyle {\ce {A}}} 3894:{\displaystyle {\ce {A}}} 2523:With non-ideal reactors, 670:and the fluid flow rate ( 80:environmental engineering 5897:Microbial biodegradation 5576:Industrial biotechnology 5536:History of biotechnology 5018: 4646:{\displaystyle {\ce {}}} 4616:{\displaystyle {\ce {}}} 27:Type of chemical reactor 5571:Colors of biotechnology 5284:Davis, Mark E. (2003). 5013:Plug flow reactor model 4933:in Greenpoint, Brooklyn 4929:Anaerobic digesters at 3352:for a desired product. 3204: 1403:A series of three CSTRs 1378:Modeling non-ideal flow 324:in a reactor of volume 135:perfect or ideal mixing 5965:Biomedical engineering 5672:Pharmaceutical company 5652:Biotechnology products 4934: 4899: 4877: 4855: 4833: 4811: 4771: 4749: 4727: 4687: 4647: 4617: 4587: 4547: 4507: 4351: 4306: 4261: 4150: 4042: 4015: 3988: 3954: 3917: 3895: 3873: 3833: 3715: 3670: 3625: 3542: 3459: 3432: 3405: 3377: 3330: 3303: 3235:Zeroth order reactions 3214: 3195: 3124: 2848: 2806: 2775: 2510: 2368: 2294: 2269: 2190: 2111: 2032: 1968: 1901: 1900:{\displaystyle C_{A1}} 1867: 1781: 1780:{\displaystyle -r_{A}} 1751: 1724: 1723:{\displaystyle C_{Ao}} 1690: 1670: 1575: 1507:Ideal cascade of CSTRs 1488: 1487:{\displaystyle F_{Ao}} 1458: 1420: 1404: 1367: 1349: 1325: 1295: 1201: 1134: 1023: 976: 940: 915: 836: 747: 654: 522: 419: 198: 110: 35: 4928: 4900: 4878: 4856: 4834: 4812: 4772: 4750: 4728: 4688: 4648: 4618: 4588: 4548: 4508: 4352: 4307: 4262: 4151: 4043: 4041:{\displaystyle k_{2}} 4016: 4014:{\displaystyle k_{1}} 3989: 3955: 3918: 3896: 3874: 3834: 3716: 3671: 3626: 3543: 3460: 3458:{\displaystyle k_{2}} 3433: 3431:{\displaystyle k_{1}} 3406: 3378: 3331: 3304: 3241:zeroth order reaction 3212: 3196: 3125: 2849: 2807: 2776: 2511: 2383:second order reaction 2369: 2295: 2249: 2208:zeroth order reaction 2191: 2112: 2033: 1969: 1902: 1868: 1782: 1752: 1750:{\displaystyle C_{A}} 1725: 1691: 1689:{\displaystyle \tau } 1671: 1576: 1489: 1459: 1425:fractional conversion 1418: 1402: 1368: 1366:{\displaystyle \tau } 1347: 1323: 1296: 1202: 1135: 1037:, the reaction rate, 1035:order of the reaction 1024: 1022:{\displaystyle \tau } 977: 941: 939:{\displaystyle \tau } 916: 837: 748: 655: 523: 420: 418:{\displaystyle 1.=-+} 273:single, irreversible 199: 108: 33: 5990:Chemical engineering 5853:Reproductive cloning 5717:Hybridoma technology 5667:Human Genome Project 4998:Laminar flow reactor 4969:Chemical engineering 4948:wastewater treatment 4887: 4865: 4843: 4821: 4787: 4759: 4737: 4697: 4657: 4627: 4597: 4557: 4517: 4513:. In the case where 4361: 4316: 4271: 4160: 4052: 4025: 3998: 3964: 3930: 3905: 3883: 3843: 3839:. In the case where 3725: 3680: 3635: 3552: 3469: 3442: 3415: 3387: 3359: 3313: 3247: 3144: 2867: 2856:volumetric flow rate 2816: 2787: 2533: 2389: 2306: 2214: 2123: 2044: 1978: 1914: 1881: 1813: 1761: 1734: 1704: 1680: 1585: 1515: 1497:first order reaction 1468: 1431: 1357: 1217: 1150: 1088: 1013: 951: 930: 847: 768: 680: 593: 576:is the reaction rate 430: 332: 144: 76:chemical engineering 5875:Genetic engineering 5858:Therapeutic cloning 5838:Bionic architecture 5818:Animal cell culture 5585:Biological concepts 5400:2015WatRe..71..282H 5248:2002LimOc..47.1545M 5199:1973Tell...25...58B 4956:Anaerobic digesters 4048:and rate equations 3465:and rate equations 3161: 1065: 343:Net accumulation of 5931:Interdisciplinary 5885:Molecular genetics 5631:Selective breeding 5439:Treatment Wetlands 4963:storm water runoff 4935: 4895: 4873: 4851: 4829: 4807: 4767: 4745: 4723: 4683: 4643: 4613: 4583: 4543: 4503: 4347: 4302: 4257: 4146: 4038: 4011: 3984: 3950: 3913: 3891: 3869: 3829: 3711: 3666: 3621: 3538: 3455: 3428: 3401: 3373: 3346:parallel reactions 3326: 3299: 3215: 3191: 3147: 3120: 2844: 2802: 2771: 2506: 2381:For an isothermal 2364: 2290: 2186: 2107: 2028: 1964: 1897: 1863: 1777: 1747: 1720: 1686: 1666: 1571: 1484: 1454: 1421: 1405: 1385:plug flow reactors 1363: 1350: 1326: 1291: 1197: 1130: 1063: 1019: 972: 970: 936: 911: 832: 743: 650: 518: 415: 194: 111: 56:mixed flow reactor 36: 6094:Chemical reactors 6081: 6080: 6010:Nanobiotechnology 6005:Molecular biology 5806: 5805: 5657:Biotechnology law 5448:978-1-56670-526-4 5372:978-0-471-25424-9 5295:978-1-62870-437-2 5145:978-1-118-63227-7 5093:978-0-07-340118-8 4893: 4871: 4849: 4827: 4805: 4799: 4793: 4765: 4743: 4637: 4607: 4471: 4433: 4425: 4398: 4392: 4376: 4345: 4331: 4300: 4286: 4235: 4210: 4189: 4175: 4127: 4102: 4081: 4067: 3982: 3976: 3970: 3948: 3942: 3936: 3911: 3889: 3797: 3789: 3762: 3756: 3740: 3709: 3695: 3664: 3650: 3602: 3581: 3567: 3519: 3498: 3484: 3399: 3393: 3371: 3365: 3344:When considering 3324: 3297: 3189: 3177: 3099: 3097: 3074: 3022: 3020: 2997: 2979: 2977: 2946: 2944: 2907: 2842: 2828: 2799: 2750: 2748: 2725: 2673: 2671: 2648: 2630: 2628: 2597: 2595: 2558: 2504: 2476: 2184: 2105: 2026: 1962: 1873:, where k is the 1861: 1664: 1569: 1452: 1411:Minimizing volume 1395:Cascades of CSTRs 1313: 1312: 1289: 1275: 1195: 1033:Depending on the 969: 877: 855: 798: 776: 688: 601: 461: 408: 404: 403:Net generation of 390: 386: 370: 366: 348: 344: 217:closed boundaries 179: 95:plug flow reactor 46:), also known as 16:(Redirected from 6101: 6069: 6068: 6057: 6056: 5907:Pharmacogenomics 5687: 5686: 5681:Basic techniques 5662:Green Revolution 5640:General concepts 5558: 5515: 5508: 5501: 5492: 5491: 5485: 5484: 5482: 5481: 5472:. Archived from 5462: 5453: 5452: 5434: 5428: 5427: 5383: 5377: 5376: 5358: 5352: 5351: 5333: 5327: 5326: 5314: 5308: 5307: 5281: 5270: 5269: 5259: 5242:(5): 1545–1553. 5227: 5221: 5220: 5210: 5178: 5172: 5171: 5165: 5157: 5131: 5120: 5119: 5113: 5105: 5079: 5056: 5055: 5037: 4944:Activated sludge 4904: 4902: 4901: 4896: 4894: 4891: 4882: 4880: 4879: 4874: 4872: 4869: 4860: 4858: 4857: 4852: 4850: 4847: 4838: 4836: 4835: 4830: 4828: 4825: 4816: 4814: 4813: 4808: 4806: 4803: 4797: 4791: 4781:Series reactions 4776: 4774: 4773: 4768: 4766: 4763: 4754: 4752: 4751: 4746: 4744: 4741: 4732: 4730: 4729: 4724: 4722: 4721: 4709: 4708: 4692: 4690: 4689: 4684: 4682: 4681: 4669: 4668: 4652: 4650: 4649: 4644: 4642: 4641: 4635: 4622: 4620: 4619: 4614: 4612: 4611: 4605: 4592: 4590: 4589: 4584: 4582: 4581: 4569: 4568: 4552: 4550: 4549: 4544: 4542: 4541: 4529: 4528: 4512: 4510: 4509: 4504: 4502: 4501: 4500: 4499: 4487: 4486: 4472: 4469: 4464: 4463: 4462: 4461: 4449: 4448: 4434: 4431: 4426: 4424: 4423: 4414: 4413: 4404: 4399: 4397: 4393: 4390: 4381: 4377: 4374: 4365: 4356: 4354: 4353: 4348: 4346: 4344: 4336: 4332: 4329: 4320: 4311: 4309: 4308: 4303: 4301: 4299: 4291: 4287: 4284: 4275: 4266: 4264: 4263: 4258: 4256: 4255: 4251: 4250: 4236: 4233: 4228: 4227: 4226: 4225: 4211: 4208: 4203: 4202: 4190: 4188: 4180: 4176: 4173: 4164: 4155: 4153: 4152: 4147: 4145: 4144: 4143: 4142: 4128: 4125: 4120: 4119: 4118: 4117: 4103: 4100: 4095: 4094: 4082: 4080: 4072: 4068: 4065: 4056: 4047: 4045: 4044: 4039: 4037: 4036: 4020: 4018: 4017: 4012: 4010: 4009: 3993: 3991: 3990: 3985: 3983: 3980: 3974: 3968: 3959: 3957: 3956: 3951: 3949: 3946: 3940: 3934: 3922: 3920: 3919: 3914: 3912: 3909: 3900: 3898: 3897: 3892: 3890: 3887: 3878: 3876: 3875: 3870: 3868: 3867: 3855: 3854: 3838: 3836: 3835: 3830: 3828: 3827: 3826: 3825: 3813: 3812: 3798: 3795: 3790: 3788: 3787: 3778: 3777: 3768: 3763: 3761: 3757: 3754: 3745: 3741: 3738: 3729: 3720: 3718: 3717: 3712: 3710: 3708: 3700: 3696: 3693: 3684: 3675: 3673: 3672: 3667: 3665: 3663: 3655: 3651: 3648: 3639: 3630: 3628: 3627: 3622: 3620: 3619: 3618: 3617: 3603: 3600: 3595: 3594: 3582: 3580: 3572: 3568: 3565: 3556: 3547: 3545: 3544: 3539: 3537: 3536: 3535: 3534: 3520: 3517: 3512: 3511: 3499: 3497: 3489: 3485: 3482: 3473: 3464: 3462: 3461: 3456: 3454: 3453: 3437: 3435: 3434: 3429: 3427: 3426: 3410: 3408: 3407: 3402: 3400: 3397: 3391: 3382: 3380: 3379: 3374: 3372: 3369: 3363: 3335: 3333: 3332: 3327: 3325: 3317: 3308: 3306: 3305: 3300: 3298: 3296: 3288: 3287: 3286: 3271: 3270: 3257: 3200: 3198: 3197: 3192: 3190: 3185: 3184: 3179: 3178: 3170: 3166: 3160: 3155: 3129: 3127: 3126: 3121: 3116: 3115: 3100: 3098: 3090: 3088: 3080: 3075: 3073: 3050: 3033: 3032: 3023: 3021: 3013: 3011: 3003: 2998: 2996: 2985: 2980: 2978: 2970: 2968: 2960: 2949: 2948: 2947: 2945: 2937: 2935: 2927: 2908: 2906: 2905: 2896: 2895: 2886: 2853: 2851: 2850: 2845: 2843: 2835: 2830: 2829: 2821: 2811: 2809: 2808: 2803: 2801: 2800: 2792: 2780: 2778: 2777: 2772: 2767: 2766: 2751: 2749: 2741: 2739: 2731: 2726: 2724: 2701: 2684: 2683: 2674: 2672: 2664: 2662: 2654: 2649: 2647: 2636: 2631: 2629: 2621: 2619: 2611: 2600: 2599: 2598: 2596: 2588: 2586: 2578: 2559: 2557: 2556: 2547: 2546: 2537: 2515: 2513: 2512: 2507: 2505: 2503: 2502: 2501: 2492: 2491: 2478: 2477: 2475: 2474: 2450: 2449: 2440: 2439: 2421: 2409: 2404: 2403: 2373: 2371: 2370: 2365: 2363: 2362: 2353: 2352: 2337: 2336: 2321: 2320: 2299: 2297: 2296: 2291: 2289: 2288: 2279: 2278: 2268: 2263: 2245: 2244: 2229: 2228: 2195: 2193: 2192: 2187: 2185: 2183: 2182: 2181: 2156: 2155: 2143: 2138: 2137: 2116: 2114: 2113: 2108: 2106: 2104: 2103: 2102: 2077: 2076: 2064: 2059: 2058: 2037: 2035: 2034: 2029: 2027: 2025: 2011: 2010: 1998: 1993: 1992: 1973: 1971: 1970: 1965: 1963: 1961: 1947: 1946: 1934: 1929: 1928: 1906: 1904: 1903: 1898: 1896: 1895: 1872: 1870: 1869: 1864: 1862: 1860: 1846: 1845: 1833: 1828: 1827: 1789:rate of reaction 1786: 1784: 1783: 1778: 1776: 1775: 1756: 1754: 1753: 1748: 1746: 1745: 1729: 1727: 1726: 1721: 1719: 1718: 1700:of the reactor, 1695: 1693: 1692: 1687: 1675: 1673: 1672: 1667: 1665: 1663: 1662: 1661: 1645: 1644: 1643: 1628: 1627: 1602: 1597: 1596: 1580: 1578: 1577: 1572: 1570: 1568: 1567: 1566: 1553: 1552: 1551: 1539: 1538: 1525: 1493: 1491: 1490: 1485: 1483: 1482: 1463: 1461: 1460: 1455: 1453: 1451: 1450: 1435: 1372: 1370: 1369: 1364: 1300: 1298: 1297: 1292: 1290: 1288: 1277: 1276: 1274: 1273: 1246: 1234: 1229: 1228: 1206: 1204: 1203: 1198: 1196: 1194: 1180: 1179: 1167: 1162: 1161: 1139: 1137: 1136: 1131: 1129: 1118: 1117: 1116: 1100: 1099: 1066: 1062: 1028: 1026: 1025: 1020: 981: 979: 978: 973: 971: 962: 945: 943: 942: 937: 920: 918: 917: 912: 907: 906: 894: 893: 878: 870: 865: 864: 853: 841: 839: 838: 833: 828: 827: 815: 814: 799: 791: 786: 785: 774: 762:and simplified: 752: 750: 749: 744: 742: 741: 726: 725: 710: 709: 686: 659: 657: 656: 651: 649: 648: 633: 632: 620: 619: 599: 527: 525: 524: 519: 517: 516: 507: 506: 491: 490: 478: 477: 462: 460: 452: 451: 450: 437: 424: 422: 421: 416: 406: 405: 402: 391: 388: 384: 371: 368: 364: 346: 345: 342: 228:n-order reaction 203: 201: 200: 195: 193: 192: 180: 178: 170: 169: 168: 155: 153: 152: 72:chemical reactor 21: 6109: 6108: 6104: 6103: 6102: 6100: 6099: 6098: 6084: 6083: 6082: 6077: 6045: 6019: 5960:Biopharmacology 5932: 5926: 5802: 5773:Electrophoresis 5768:Kidney dialysis 5758:Crystallization 5736: 5682: 5676: 5635: 5580: 5559: 5550: 5524: 5519: 5489: 5488: 5479: 5477: 5464: 5463: 5456: 5449: 5435: 5431: 5384: 5380: 5373: 5359: 5355: 5348: 5334: 5330: 5315: 5311: 5296: 5282: 5273: 5228: 5224: 5179: 5175: 5159: 5158: 5146: 5132: 5123: 5107: 5106: 5094: 5080: 5059: 5052: 5038: 5031: 5026: 5021: 4994: 4971: 4940: 4919: 4890: 4888: 4885: 4884: 4868: 4866: 4863: 4862: 4846: 4844: 4841: 4840: 4824: 4822: 4819: 4818: 4790: 4788: 4785: 4784: 4762: 4760: 4757: 4756: 4740: 4738: 4735: 4734: 4717: 4713: 4704: 4700: 4698: 4695: 4694: 4677: 4673: 4664: 4660: 4658: 4655: 4654: 4631: 4630: 4628: 4625: 4624: 4601: 4600: 4598: 4595: 4594: 4577: 4573: 4564: 4560: 4558: 4555: 4554: 4537: 4533: 4524: 4520: 4518: 4515: 4514: 4495: 4491: 4482: 4478: 4477: 4473: 4468: 4457: 4453: 4444: 4440: 4439: 4435: 4430: 4419: 4415: 4409: 4405: 4403: 4389: 4382: 4373: 4366: 4364: 4362: 4359: 4358: 4337: 4328: 4321: 4319: 4317: 4314: 4313: 4292: 4283: 4276: 4274: 4272: 4269: 4268: 4246: 4242: 4241: 4237: 4232: 4221: 4217: 4216: 4212: 4207: 4198: 4194: 4181: 4172: 4165: 4163: 4161: 4158: 4157: 4138: 4134: 4133: 4129: 4124: 4113: 4109: 4108: 4104: 4099: 4090: 4086: 4073: 4064: 4057: 4055: 4053: 4050: 4049: 4032: 4028: 4026: 4023: 4022: 4005: 4001: 3999: 3996: 3995: 3994:with constants 3967: 3965: 3962: 3961: 3933: 3931: 3928: 3927: 3908: 3906: 3903: 3902: 3886: 3884: 3881: 3880: 3863: 3859: 3850: 3846: 3844: 3841: 3840: 3821: 3817: 3808: 3804: 3803: 3799: 3794: 3783: 3779: 3773: 3769: 3767: 3753: 3746: 3737: 3730: 3728: 3726: 3723: 3722: 3701: 3692: 3685: 3683: 3681: 3678: 3677: 3656: 3647: 3640: 3638: 3636: 3633: 3632: 3613: 3609: 3608: 3604: 3599: 3590: 3586: 3573: 3564: 3557: 3555: 3553: 3550: 3549: 3530: 3526: 3525: 3521: 3516: 3507: 3503: 3490: 3481: 3474: 3472: 3470: 3467: 3466: 3449: 3445: 3443: 3440: 3439: 3422: 3418: 3416: 3413: 3412: 3411:with constants 3390: 3388: 3385: 3384: 3362: 3360: 3357: 3356: 3342: 3316: 3314: 3311: 3310: 3289: 3279: 3275: 3263: 3259: 3258: 3256: 3248: 3245: 3244: 3237: 3223:operating costs 3207: 3180: 3169: 3168: 3167: 3165: 3156: 3151: 3145: 3142: 3141: 3105: 3101: 3089: 3081: 3079: 3054: 3049: 3028: 3024: 3012: 3004: 3002: 2989: 2984: 2969: 2961: 2959: 2936: 2928: 2926: 2922: 2918: 2901: 2897: 2891: 2887: 2885: 2868: 2865: 2864: 2854:where Q is the 2834: 2820: 2819: 2817: 2814: 2813: 2791: 2790: 2788: 2785: 2784: 2756: 2752: 2740: 2732: 2730: 2705: 2700: 2679: 2675: 2663: 2655: 2653: 2640: 2635: 2620: 2612: 2610: 2587: 2579: 2577: 2573: 2569: 2552: 2548: 2542: 2538: 2536: 2534: 2531: 2530: 2521: 2497: 2493: 2487: 2483: 2479: 2455: 2451: 2445: 2441: 2435: 2431: 2420: 2410: 2408: 2396: 2392: 2390: 2387: 2386: 2379: 2358: 2354: 2348: 2344: 2329: 2325: 2313: 2309: 2307: 2304: 2303: 2284: 2280: 2274: 2270: 2264: 2253: 2237: 2233: 2221: 2217: 2215: 2212: 2211: 2204: 2177: 2173: 2157: 2148: 2144: 2142: 2130: 2126: 2124: 2121: 2120: 2098: 2094: 2078: 2069: 2065: 2063: 2051: 2047: 2045: 2042: 2041: 2012: 2003: 1999: 1997: 1985: 1981: 1979: 1976: 1975: 1948: 1939: 1935: 1933: 1921: 1917: 1915: 1912: 1911: 1888: 1884: 1882: 1879: 1878: 1847: 1838: 1834: 1832: 1820: 1816: 1814: 1811: 1810: 1797: 1771: 1767: 1762: 1759: 1758: 1741: 1737: 1735: 1732: 1731: 1711: 1707: 1705: 1702: 1701: 1681: 1678: 1677: 1654: 1650: 1646: 1636: 1632: 1608: 1604: 1603: 1601: 1592: 1588: 1586: 1583: 1582: 1562: 1558: 1554: 1547: 1543: 1531: 1527: 1526: 1524: 1516: 1513: 1512: 1509: 1475: 1471: 1469: 1466: 1465: 1443: 1439: 1434: 1432: 1429: 1428: 1413: 1397: 1380: 1358: 1355: 1354: 1338: 1318: 1309: 1278: 1266: 1262: 1245: 1235: 1233: 1224: 1220: 1218: 1215: 1214: 1181: 1172: 1168: 1166: 1157: 1153: 1151: 1148: 1147: 1122: 1109: 1105: 1104: 1095: 1091: 1089: 1086: 1085: 1076: 1069:Reaction Order 1042: 1014: 1011: 1010: 999: 990: 960: 952: 949: 948: 931: 928: 927: 902: 898: 886: 882: 869: 860: 856: 848: 845: 844: 823: 819: 807: 803: 790: 781: 777: 769: 766: 765: 760: 737: 733: 721: 717: 702: 698: 681: 678: 677: 644: 640: 628: 624: 612: 608: 594: 591: 590: 585: 574: 562: 550: 538: 512: 508: 502: 498: 486: 482: 470: 466: 453: 446: 442: 438: 436: 431: 428: 427: 401: 387: 367: 341: 333: 330: 329: 318: 305: 298: 282: 250: 239: 220:constant fluid 209: 188: 187: 171: 164: 160: 156: 154: 148: 147: 145: 142: 141: 116: 103: 52:backmix reactor 28: 23: 22: 15: 12: 11: 5: 6107: 6097: 6096: 6079: 6078: 6076: 6075: 6063: 6050: 6047: 6046: 6044: 6043: 6038: 6033: 6027: 6025: 6021: 6020: 6018: 6017: 6012: 6007: 6002: 5997: 5992: 5987: 5982: 5977: 5972: 5967: 5962: 5957: 5952: 5950:Bioengineering 5947: 5945:Bioelectronics 5942: 5936: 5934: 5928: 5927: 5925: 5924: 5922:Tissue culture 5919: 5914: 5909: 5904: 5899: 5894: 5889: 5888: 5887: 5882: 5872: 5867: 5862: 5861: 5860: 5855: 5845: 5840: 5835: 5830: 5828:Bioinformatics 5825: 5823:Biofabrication 5820: 5814: 5812: 5808: 5807: 5804: 5803: 5801: 5800: 5795: 5790: 5785: 5780: 5775: 5770: 5765: 5763:Chromatography 5760: 5755: 5750: 5748:Centrifugation 5744: 5742: 5741:Chemical field 5738: 5737: 5735: 5734: 5729: 5724: 5719: 5714: 5712:Flow cytometry 5709: 5704: 5699: 5693: 5691: 5684: 5678: 5677: 5675: 5674: 5669: 5664: 5659: 5654: 5649: 5643: 5641: 5637: 5636: 5634: 5633: 5628: 5623: 5618: 5613: 5608: 5599: 5594: 5588: 5586: 5582: 5581: 5579: 5578: 5573: 5567: 5565: 5561: 5560: 5553: 5551: 5549: 5548: 5543: 5538: 5532: 5530: 5526: 5525: 5518: 5517: 5510: 5503: 5495: 5487: 5486: 5454: 5447: 5429: 5388:Water Research 5378: 5371: 5353: 5346: 5328: 5309: 5294: 5271: 5222: 5173: 5144: 5121: 5092: 5057: 5050: 5028: 5027: 5025: 5022: 5020: 5017: 5016: 5015: 5010: 5005: 5000: 4993: 4990: 4989: 4988: 4982: 4976: 4975: 4970: 4967: 4966: 4965: 4959: 4953: 4950: 4939: 4936: 4918: 4915: 4905:. Typically a 4802: 4796: 4720: 4716: 4712: 4707: 4703: 4680: 4676: 4672: 4667: 4663: 4640: 4634: 4610: 4604: 4580: 4576: 4572: 4567: 4563: 4540: 4536: 4532: 4527: 4523: 4498: 4494: 4490: 4485: 4481: 4476: 4467: 4460: 4456: 4452: 4447: 4443: 4438: 4429: 4422: 4418: 4412: 4408: 4402: 4396: 4388: 4385: 4380: 4372: 4369: 4343: 4340: 4335: 4327: 4324: 4298: 4295: 4290: 4282: 4279: 4254: 4249: 4245: 4240: 4231: 4224: 4220: 4215: 4206: 4201: 4197: 4193: 4187: 4184: 4179: 4171: 4168: 4141: 4137: 4132: 4123: 4116: 4112: 4107: 4098: 4093: 4089: 4085: 4079: 4076: 4071: 4063: 4060: 4035: 4031: 4008: 4004: 3979: 3973: 3945: 3939: 3866: 3862: 3858: 3853: 3849: 3824: 3820: 3816: 3811: 3807: 3802: 3793: 3786: 3782: 3776: 3772: 3766: 3760: 3752: 3749: 3744: 3736: 3733: 3707: 3704: 3699: 3691: 3688: 3662: 3659: 3654: 3646: 3643: 3616: 3612: 3607: 3598: 3593: 3589: 3585: 3579: 3576: 3571: 3563: 3560: 3533: 3529: 3524: 3515: 3510: 3506: 3502: 3496: 3493: 3488: 3480: 3477: 3452: 3448: 3425: 3421: 3396: 3368: 3341: 3338: 3323: 3320: 3295: 3292: 3285: 3282: 3278: 3274: 3269: 3266: 3262: 3255: 3252: 3236: 3233: 3206: 3203: 3188: 3183: 3176: 3173: 3164: 3159: 3154: 3150: 3138:pulse stimulus 3119: 3114: 3111: 3108: 3104: 3096: 3093: 3087: 3084: 3078: 3072: 3069: 3066: 3063: 3060: 3057: 3053: 3048: 3045: 3042: 3039: 3036: 3031: 3027: 3019: 3016: 3010: 3007: 3001: 2995: 2992: 2988: 2983: 2976: 2973: 2967: 2964: 2958: 2955: 2952: 2943: 2940: 2934: 2931: 2925: 2921: 2917: 2914: 2911: 2904: 2900: 2894: 2890: 2884: 2881: 2878: 2875: 2872: 2841: 2838: 2833: 2827: 2824: 2798: 2795: 2770: 2765: 2762: 2759: 2755: 2747: 2744: 2738: 2735: 2729: 2723: 2720: 2717: 2714: 2711: 2708: 2704: 2699: 2696: 2693: 2690: 2687: 2682: 2678: 2670: 2667: 2661: 2658: 2652: 2646: 2643: 2639: 2634: 2627: 2624: 2618: 2615: 2609: 2606: 2603: 2594: 2591: 2585: 2582: 2576: 2572: 2568: 2565: 2562: 2555: 2551: 2545: 2541: 2520: 2517: 2500: 2496: 2490: 2486: 2482: 2473: 2470: 2467: 2464: 2461: 2458: 2454: 2448: 2444: 2438: 2434: 2430: 2427: 2424: 2419: 2416: 2413: 2407: 2402: 2399: 2395: 2378: 2375: 2361: 2357: 2351: 2347: 2343: 2340: 2335: 2332: 2328: 2324: 2319: 2316: 2312: 2287: 2283: 2277: 2273: 2267: 2262: 2259: 2256: 2252: 2248: 2243: 2240: 2236: 2232: 2227: 2224: 2220: 2203: 2200: 2180: 2176: 2172: 2169: 2166: 2163: 2160: 2154: 2151: 2147: 2141: 2136: 2133: 2129: 2101: 2097: 2093: 2090: 2087: 2084: 2081: 2075: 2072: 2068: 2062: 2057: 2054: 2050: 2024: 2021: 2018: 2015: 2009: 2006: 2002: 1996: 1991: 1988: 1984: 1960: 1957: 1954: 1951: 1945: 1942: 1938: 1932: 1927: 1924: 1920: 1894: 1891: 1887: 1859: 1856: 1853: 1850: 1844: 1841: 1837: 1831: 1826: 1823: 1819: 1809:For one CSTR: 1796: 1793: 1774: 1770: 1766: 1744: 1740: 1717: 1714: 1710: 1685: 1660: 1657: 1653: 1649: 1642: 1639: 1635: 1631: 1626: 1623: 1620: 1617: 1614: 1611: 1607: 1600: 1595: 1591: 1565: 1561: 1557: 1550: 1546: 1542: 1537: 1534: 1530: 1523: 1520: 1508: 1505: 1481: 1478: 1474: 1449: 1446: 1442: 1438: 1412: 1409: 1396: 1393: 1379: 1376: 1362: 1337: 1336:Non-ideal CSTR 1334: 1317: 1314: 1311: 1310: 1306: 1302: 1301: 1287: 1284: 1281: 1272: 1269: 1265: 1261: 1258: 1255: 1252: 1249: 1244: 1241: 1238: 1232: 1227: 1223: 1212: 1208: 1207: 1193: 1190: 1187: 1184: 1178: 1175: 1171: 1165: 1160: 1156: 1145: 1141: 1140: 1128: 1125: 1121: 1115: 1112: 1108: 1103: 1098: 1094: 1083: 1079: 1078: 1074: 1070: 1040: 1018: 1006:Residence time 1003: 1002: 997: 993: 988: 984: 968: 965: 959: 956: 935: 910: 905: 901: 897: 892: 889: 885: 881: 876: 873: 868: 863: 859: 852: 831: 826: 822: 818: 813: 810: 806: 802: 797: 794: 789: 784: 780: 773: 758: 740: 736: 732: 729: 724: 720: 716: 713: 708: 705: 701: 697: 694: 691: 685: 647: 643: 639: 636: 631: 627: 623: 618: 615: 611: 607: 604: 598: 583: 578: 577: 572: 568: 560: 556: 548: 544: 536: 515: 511: 505: 501: 497: 494: 489: 485: 481: 476: 473: 469: 465: 459: 456: 449: 445: 441: 435: 414: 411: 400: 397: 394: 383: 380: 377: 374: 363: 360: 357: 354: 351: 340: 337: 316: 311: 310: 303: 296: 292: 285: 280: 271: 261: 248: 237: 225: 218: 215: 207: 191: 186: 183: 177: 174: 167: 163: 159: 151: 136: 115: 112: 102: 99: 91:perfect mixing 26: 9: 6: 4: 3: 2: 6106: 6095: 6092: 6091: 6089: 6074: 6073: 6064: 6062: 6061: 6052: 6051: 6048: 6042: 6039: 6037: 6034: 6032: 6029: 6028: 6026: 6022: 6016: 6013: 6011: 6008: 6006: 6003: 6001: 5998: 5996: 5993: 5991: 5988: 5986: 5983: 5981: 5978: 5976: 5973: 5971: 5968: 5966: 5963: 5961: 5958: 5956: 5953: 5951: 5948: 5946: 5943: 5941: 5938: 5937: 5935: 5929: 5923: 5920: 5918: 5915: 5913: 5910: 5908: 5905: 5903: 5900: 5898: 5895: 5893: 5890: 5886: 5883: 5881: 5878: 5877: 5876: 5873: 5871: 5868: 5866: 5863: 5859: 5856: 5854: 5851: 5850: 5849: 5846: 5844: 5843:Cell immunity 5841: 5839: 5836: 5834: 5831: 5829: 5826: 5824: 5821: 5819: 5816: 5815: 5813: 5809: 5799: 5798:Sedimentation 5796: 5794: 5791: 5789: 5786: 5784: 5781: 5779: 5776: 5774: 5771: 5769: 5766: 5764: 5761: 5759: 5756: 5754: 5751: 5749: 5746: 5745: 5743: 5739: 5733: 5730: 5728: 5725: 5723: 5720: 5718: 5715: 5713: 5710: 5708: 5707:Cultured meat 5705: 5703: 5700: 5698: 5695: 5694: 5692: 5690:Biology field 5688: 5685: 5679: 5673: 5670: 5668: 5665: 5663: 5660: 5658: 5655: 5653: 5650: 5648: 5645: 5644: 5642: 5638: 5632: 5629: 5627: 5624: 5622: 5619: 5617: 5614: 5612: 5609: 5607: 5603: 5600: 5598: 5595: 5593: 5590: 5589: 5587: 5583: 5577: 5574: 5572: 5569: 5568: 5566: 5562: 5557: 5547: 5544: 5542: 5539: 5537: 5534: 5533: 5531: 5527: 5523: 5522:Biotechnology 5516: 5511: 5509: 5504: 5502: 5497: 5496: 5493: 5476:on 2013-12-14 5475: 5471: 5467: 5461: 5459: 5450: 5444: 5440: 5433: 5425: 5421: 5417: 5413: 5409: 5405: 5401: 5397: 5393: 5389: 5382: 5374: 5368: 5364: 5357: 5349: 5347:9781118368251 5343: 5339: 5332: 5325:(6): 723–725. 5324: 5320: 5313: 5305: 5301: 5297: 5291: 5287: 5280: 5278: 5276: 5267: 5263: 5258: 5253: 5249: 5245: 5241: 5237: 5233: 5226: 5218: 5214: 5209: 5204: 5200: 5196: 5192: 5188: 5184: 5177: 5169: 5163: 5155: 5151: 5147: 5141: 5137: 5130: 5128: 5126: 5117: 5111: 5103: 5099: 5095: 5089: 5085: 5078: 5076: 5074: 5072: 5070: 5068: 5066: 5064: 5062: 5053: 5051:0-19-510588-5 5047: 5043: 5036: 5034: 5029: 5014: 5011: 5009: 5006: 5004: 5001: 4999: 4996: 4995: 4986: 4983: 4981: 4978: 4977: 4973: 4972: 4964: 4960: 4957: 4954: 4951: 4949: 4945: 4942: 4941: 4932: 4927: 4923: 4914: 4912: 4908: 4907:batch reactor 4782: 4778: 4718: 4714: 4710: 4705: 4701: 4678: 4674: 4670: 4665: 4661: 4578: 4574: 4570: 4565: 4561: 4538: 4534: 4530: 4525: 4521: 4496: 4492: 4488: 4483: 4479: 4458: 4454: 4450: 4445: 4441: 4420: 4416: 4410: 4406: 4400: 4383: 4367: 4341: 4338: 4322: 4296: 4293: 4277: 4252: 4247: 4243: 4222: 4218: 4199: 4195: 4191: 4185: 4182: 4166: 4139: 4135: 4114: 4110: 4091: 4087: 4083: 4077: 4074: 4058: 4033: 4029: 4006: 4002: 3971: 3937: 3924: 3864: 3860: 3856: 3851: 3847: 3822: 3818: 3814: 3809: 3805: 3784: 3780: 3774: 3770: 3764: 3747: 3731: 3705: 3702: 3686: 3660: 3657: 3641: 3614: 3610: 3591: 3587: 3583: 3577: 3574: 3558: 3531: 3527: 3508: 3504: 3500: 3494: 3491: 3475: 3450: 3446: 3423: 3419: 3353: 3351: 3347: 3337: 3321: 3318: 3293: 3290: 3283: 3280: 3276: 3272: 3267: 3264: 3260: 3253: 3250: 3242: 3232: 3229: 3224: 3220: 3211: 3202: 3186: 3181: 3171: 3162: 3157: 3152: 3148: 3139: 3135: 3130: 3112: 3109: 3106: 3091: 3085: 3082: 3070: 3064: 3061: 3058: 3051: 3046: 3043: 3040: 3037: 3034: 3029: 3014: 3008: 3005: 2993: 2990: 2986: 2981: 2971: 2965: 2962: 2956: 2953: 2938: 2932: 2929: 2923: 2919: 2915: 2912: 2909: 2902: 2898: 2892: 2888: 2882: 2876: 2870: 2862: 2859: 2857: 2839: 2836: 2831: 2822: 2793: 2781: 2763: 2760: 2757: 2742: 2736: 2733: 2721: 2715: 2712: 2709: 2702: 2697: 2694: 2691: 2688: 2685: 2680: 2665: 2659: 2656: 2644: 2641: 2637: 2632: 2622: 2616: 2613: 2607: 2604: 2589: 2583: 2580: 2574: 2570: 2566: 2563: 2560: 2553: 2549: 2543: 2539: 2528: 2526: 2516: 2498: 2494: 2488: 2484: 2480: 2468: 2465: 2462: 2456: 2452: 2446: 2442: 2436: 2432: 2428: 2425: 2422: 2417: 2414: 2411: 2405: 2400: 2397: 2393: 2384: 2374: 2359: 2355: 2349: 2345: 2341: 2338: 2333: 2330: 2326: 2322: 2317: 2314: 2310: 2300: 2285: 2281: 2275: 2271: 2265: 2260: 2257: 2254: 2250: 2246: 2241: 2238: 2234: 2230: 2225: 2222: 2218: 2209: 2199: 2196: 2178: 2170: 2167: 2164: 2161: 2152: 2149: 2145: 2139: 2134: 2131: 2127: 2117: 2099: 2091: 2088: 2085: 2082: 2073: 2070: 2066: 2060: 2055: 2052: 2048: 2038: 2022: 2019: 2016: 2013: 2007: 2004: 2000: 1994: 1989: 1986: 1982: 1958: 1955: 1952: 1949: 1943: 1940: 1936: 1930: 1925: 1922: 1918: 1908: 1892: 1889: 1885: 1876: 1875:rate constant 1857: 1854: 1851: 1848: 1842: 1839: 1835: 1829: 1824: 1821: 1817: 1807: 1806: 1802: 1792: 1790: 1772: 1768: 1764: 1742: 1738: 1715: 1712: 1708: 1699: 1683: 1658: 1655: 1651: 1647: 1640: 1637: 1633: 1629: 1621: 1618: 1615: 1609: 1605: 1598: 1593: 1589: 1563: 1559: 1555: 1548: 1544: 1540: 1535: 1532: 1528: 1521: 1518: 1504: 1502: 1498: 1479: 1476: 1472: 1447: 1444: 1440: 1436: 1426: 1417: 1408: 1401: 1392: 1388: 1386: 1375: 1373: 1360: 1346: 1342: 1333: 1331: 1322: 1307: 1304: 1303: 1285: 1282: 1279: 1270: 1267: 1263: 1259: 1256: 1253: 1250: 1247: 1242: 1239: 1236: 1230: 1225: 1221: 1213: 1210: 1209: 1191: 1188: 1185: 1182: 1176: 1173: 1169: 1163: 1158: 1154: 1146: 1143: 1142: 1126: 1123: 1119: 1113: 1110: 1106: 1101: 1096: 1092: 1084: 1081: 1080: 1077: 1071: 1068: 1067: 1061: 1059: 1054: 1052: 1047: 1043: 1036: 1031: 1029: 1016: 1007: 1000: 994: 991: 985: 982: 966: 963: 957: 954: 933: 926: 925: 924: 921: 903: 899: 895: 890: 887: 883: 874: 871: 866: 861: 857: 850: 842: 824: 820: 816: 811: 808: 804: 795: 792: 787: 782: 778: 771: 763: 761: 753: 738: 734: 730: 727: 722: 718: 714: 711: 706: 703: 699: 695: 692: 689: 683: 675: 673: 669: 665: 660: 645: 641: 637: 634: 629: 625: 621: 616: 613: 609: 605: 602: 596: 588: 586: 575: 569: 567: 563: 557: 555: 551: 545: 543: 539: 533: 532: 531: 528: 513: 509: 503: 499: 495: 492: 487: 483: 479: 474: 471: 467: 463: 457: 454: 447: 443: 439: 433: 425: 409: 395: 381: 375: 361: 355: 349: 335: 327: 323: 319: 309: 306: 299: 293: 290: 287:All reactant 286: 283: 276: 272: 269: 265: 262: 259: 255: 251: 244: 240: 233: 229: 226: 223: 219: 216: 214: 210: 184: 181: 175: 172: 165: 161: 157: 140: 137: 134: 133: 132: 131: 127: 125: 121: 107: 98: 96: 92: 87: 85: 81: 77: 73: 69: 65: 61: 57: 53: 49: 45: 41: 32: 19: 6070: 6058: 5995:Microbiology 5980:Biochemicals 5892:Gene therapy 5833:Biosynthesis 5811:Applications 5752: 5732:Spectroscopy 5702:Cell culture 5611:Fermentation 5478:. Retrieved 5474:the original 5469: 5438: 5432: 5391: 5387: 5381: 5362: 5356: 5337: 5331: 5322: 5318: 5312: 5285: 5239: 5235: 5225: 5193:(1): 58–62. 5190: 5186: 5176: 5135: 5083: 5041: 5003:Microreactor 4980:Fermentation 4946:process for 4920: 4917:Applications 4779: 4777:is favored. 4357:. Therefore 3925: 3721:. Therefore 3354: 3343: 3238: 3216: 3131: 2863: 2860: 2782: 2529: 2522: 2380: 2377:Second order 2301: 2205: 2202:Zeroth order 2197: 2118: 2039: 1909: 1808: 1805:steady state 1798: 1510: 1422: 1406: 1389: 1381: 1353: 1351: 1339: 1327: 1072: 1057: 1055: 1045: 1038: 1032: 1009: 1004: 995: 986: 947: 922: 843: 764: 756: 754: 676: 671: 667: 663: 661: 589: 581: 579: 570: 558: 553: 546: 541: 534: 529: 426: 325: 321: 314: 312: 307: 301: 294: 288: 278: 270:is constant) 267: 257: 253: 246: 242: 235: 231: 212: 205: 139:steady state 130:Assumptions: 129: 128: 123: 119: 117: 88: 67: 63: 59: 55: 51: 47: 43: 39: 37: 5985:Biorobotics 5975:Biomimetics 5970:Biomedicine 5394:: 282–293. 3350:selectivity 1910:Two CSTRs: 1795:First order 320:of species 5940:Bioeconomy 5912:Stem cells 5865:Embryology 5788:Filtration 5778:Extraction 5697:Bioreactor 5480:2020-04-30 5024:References 4987:production 1801:isothermal 1698:space time 264:isothermal 101:Ideal CSTR 5783:Fed Batch 5683:and tools 5416:0043-1354 5365:. Wiley. 5304:880604539 5217:0040-2826 5162:cite book 5154:856567226 5110:cite book 5102:858915999 4801:⟶ 4795:⟶ 4489:− 4451:− 3978:⟶ 3944:⟶ 3815:− 3395:⟶ 3367:⟶ 3273:− 3251:τ 3175:¯ 3149:σ 3110:− 3095:¯ 3062:− 3018:¯ 2975:¯ 2942:¯ 2924:− 2916:− 2826:¯ 2797:¯ 2761:− 2746:¯ 2713:− 2669:¯ 2626:¯ 2593:¯ 2575:− 2567:− 2495:τ 2466:− 2443:τ 2412:− 2356:τ 2339:− 2282:τ 2251:∑ 2247:− 2171:τ 2092:τ 2023:τ 1959:τ 1858:τ 1765:− 1684:τ 1648:− 1630:− 1619:− 1590:τ 1556:− 1541:− 1519:τ 1361:τ 1286:τ 1260:τ 1237:− 1192:τ 1127:τ 1120:− 1017:τ 955:τ 934:τ 896:− 875:τ 817:− 728:− 712:− 635:− 622:− 500:ν 480:− 376:− 241:), where 6088:Category 6060:Category 6015:Virology 5917:Telomere 5564:Branches 5424:25635665 5266:11505988 4992:See also 4783:such as 3134:variance 1676:, where 1305:Other n 275:reaction 204:, where 114:Modeling 84:slurries 62:), or a 6072:Commons 5955:Biology 5848:Cloning 5626:Protein 5621:Plasmid 5529:History 5396:Bibcode 5244:Bibcode 5195:Bibcode 3219:capital 1799:For an 1787:is the 1696:is the 564:is the 222:density 6000:Mining 5933:fields 5592:Allele 5445:  5422:  5414:  5369:  5344:  5302:  5292:  5264:  5215:  5187:Tellus 5152:  5142:  5100:  5090:  5048:  4985:Biogas 4156:and 3548:and 1791:of A. 923:where 854:  775:  687:  600:  530:where 407:  385:  365:  347:  6024:Lists 5902:Omics 5262:S2CID 5019:Notes 3228:pumps 284:= −1) 68:CFSTR 5753:CSTR 5722:HPLC 5616:Gene 5597:Cell 5443:ISBN 5420:PMID 5412:ISSN 5367:ISBN 5342:ISBN 5300:OCLC 5290:ISBN 5213:ISSN 5168:link 5150:OCLC 5140:ISBN 5116:link 5098:OCLC 5088:ISBN 5046:ISBN 4839:and 4711:< 4693:and 4671:> 4623:and 4571:> 4553:and 4531:> 4021:and 3960:and 3857:> 3438:and 3383:and 3221:and 3205:Cost 1974:and 1877:and 1211:n=2 1144:n=1 1082:n=0 256:and 78:and 48:vat- 44:CSTR 38:The 5793:PFR 5727:NMR 5606:RNA 5602:DNA 5404:doi 5252:doi 5203:doi 4911:PFR 4909:or 4312:by 3676:by 1501:PFR 674:): 389:out 74:in 60:MFR 50:or 6090:: 5468:. 5457:^ 5418:. 5410:. 5402:. 5392:71 5390:. 5323:48 5321:. 5298:. 5274:^ 5260:. 5250:. 5240:47 5238:. 5234:. 5211:. 5201:. 5191:25 5189:. 5185:. 5164:}} 5160:{{ 5148:. 5124:^ 5112:}} 5108:{{ 5096:. 5060:^ 5032:^ 3923:. 3243:: 3201:. 2858:. 989:Ao 851:6. 772:5. 684:4. 597:3. 537:Ao 434:2. 369:in 336:1. 300:= 254:A, 236:kC 234:= 126:. 86:. 54:, 5604:/ 5514:e 5507:t 5500:v 5483:. 5451:. 5426:. 5406:: 5398:: 5375:. 5350:. 5306:. 5268:. 5254:: 5246:: 5219:. 5205:: 5197:: 5170:) 5156:. 5118:) 5104:. 5054:. 4892:C 4870:B 4848:C 4826:B 4804:C 4798:B 4792:A 4764:D 4742:A 4719:2 4715:m 4706:1 4702:m 4679:2 4675:n 4666:1 4662:n 4639:] 4636:D 4633:[ 4609:] 4606:A 4603:[ 4579:2 4575:m 4566:1 4562:m 4539:2 4535:n 4526:1 4522:n 4497:2 4493:m 4484:1 4480:m 4475:] 4470:D 4466:[ 4459:2 4455:n 4446:1 4442:n 4437:] 4432:A 4428:[ 4421:2 4417:k 4411:1 4407:k 4401:= 4395:] 4391:C 4387:[ 4384:d 4379:] 4375:B 4371:[ 4368:d 4342:t 4339:d 4334:] 4330:C 4326:[ 4323:d 4297:t 4294:d 4289:] 4285:B 4281:[ 4278:d 4253:2 4248:1 4244:m 4239:] 4234:D 4230:[ 4223:2 4219:n 4214:] 4209:A 4205:[ 4200:2 4196:k 4192:= 4186:t 4183:d 4178:] 4174:C 4170:[ 4167:d 4140:1 4136:m 4131:] 4126:D 4122:[ 4115:1 4111:n 4106:] 4101:A 4097:[ 4092:1 4088:k 4084:= 4078:t 4075:d 4070:] 4066:B 4062:[ 4059:d 4034:2 4030:k 4007:1 4003:k 3981:C 3975:D 3972:+ 3969:A 3947:B 3941:D 3938:+ 3935:A 3910:A 3888:A 3865:2 3861:n 3852:1 3848:n 3823:2 3819:n 3810:1 3806:n 3801:] 3796:A 3792:[ 3785:2 3781:k 3775:1 3771:k 3765:= 3759:] 3755:C 3751:[ 3748:d 3743:] 3739:B 3735:[ 3732:d 3706:t 3703:d 3698:] 3694:C 3690:[ 3687:d 3661:t 3658:d 3653:] 3649:B 3645:[ 3642:d 3615:2 3611:n 3606:] 3601:A 3597:[ 3592:2 3588:k 3584:= 3578:t 3575:d 3570:] 3566:C 3562:[ 3559:d 3532:1 3528:n 3523:] 3518:A 3514:[ 3509:1 3505:k 3501:= 3495:t 3492:d 3487:] 3483:B 3479:[ 3476:d 3451:2 3447:k 3424:1 3420:k 3398:C 3392:A 3370:B 3364:A 3322:m 3319:1 3294:k 3291:m 3284:m 3281:A 3277:C 3268:o 3265:A 3261:C 3254:= 3187:n 3182:2 3172:t 3163:= 3158:2 3153:t 3118:] 3113:1 3107:n 3103:) 3092:t 3086:t 3083:n 3077:( 3071:! 3068:) 3065:1 3059:n 3056:( 3052:1 3047:+ 3044:. 3041:. 3038:. 3035:+ 3030:2 3026:) 3015:t 3009:t 3006:n 3000:( 2994:! 2991:2 2987:1 2982:+ 2972:t 2966:t 2963:n 2957:+ 2954:1 2951:[ 2939:t 2933:t 2930:n 2920:e 2913:1 2910:= 2903:o 2899:C 2893:n 2889:C 2883:= 2880:) 2877:t 2874:( 2871:F 2840:Q 2837:V 2832:= 2823:t 2794:t 2769:] 2764:1 2758:j 2754:) 2743:t 2737:t 2734:n 2728:( 2722:! 2719:) 2716:1 2710:j 2707:( 2703:1 2698:+ 2695:. 2692:. 2689:. 2686:+ 2681:2 2677:) 2666:t 2660:t 2657:n 2651:( 2645:! 2642:2 2638:1 2633:+ 2623:t 2617:t 2614:n 2608:+ 2605:1 2602:[ 2590:t 2584:t 2581:n 2571:e 2564:1 2561:= 2554:o 2550:C 2544:j 2540:C 2499:i 2489:i 2485:k 2481:2 2472:) 2469:1 2463:i 2460:( 2457:A 2453:C 2447:i 2437:i 2433:k 2429:4 2426:+ 2423:1 2418:+ 2415:1 2406:= 2401:i 2398:A 2394:C 2360:i 2350:i 2346:k 2342:m 2334:o 2331:A 2327:C 2323:= 2318:m 2315:A 2311:C 2286:i 2276:i 2272:k 2266:m 2261:1 2258:= 2255:i 2242:o 2239:A 2235:C 2231:= 2226:m 2223:A 2219:C 2179:m 2175:) 2168:k 2165:+ 2162:1 2159:( 2153:o 2150:A 2146:C 2140:= 2135:m 2132:A 2128:C 2100:2 2096:) 2089:k 2086:+ 2083:1 2080:( 2074:o 2071:A 2067:C 2061:= 2056:2 2053:A 2049:C 2020:k 2017:+ 2014:1 2008:1 2005:A 2001:C 1995:= 1990:2 1987:A 1983:C 1956:k 1953:+ 1950:1 1944:o 1941:A 1937:C 1931:= 1926:1 1923:A 1919:C 1893:1 1890:A 1886:C 1855:k 1852:+ 1849:1 1843:o 1840:A 1836:C 1830:= 1825:1 1822:A 1818:C 1773:A 1769:r 1743:A 1739:C 1716:o 1713:A 1709:C 1659:i 1656:A 1652:r 1641:i 1638:A 1634:C 1625:) 1622:1 1616:i 1613:( 1610:A 1606:C 1599:= 1594:i 1564:A 1560:r 1549:A 1545:C 1536:o 1533:A 1529:C 1522:= 1480:o 1477:A 1473:F 1448:o 1445:A 1441:F 1437:V 1283:k 1280:2 1271:o 1268:A 1264:C 1257:k 1254:4 1251:+ 1248:1 1243:+ 1240:1 1231:= 1226:A 1222:C 1189:k 1186:+ 1183:1 1177:o 1174:A 1170:C 1164:= 1159:A 1155:C 1124:k 1114:o 1111:A 1107:C 1102:= 1097:A 1093:C 1075:A 1073:C 1058:A 1046:A 1041:A 1039:r 998:A 996:C 987:C 983:) 967:Q 964:V 958:= 909:) 904:A 900:C 891:o 888:A 884:C 880:( 872:1 867:= 862:A 858:r 830:) 825:A 821:C 812:o 809:A 805:C 801:( 796:V 793:Q 788:= 783:A 779:r 759:A 757:r 739:A 735:r 731:V 723:A 719:C 715:Q 707:o 704:A 700:C 696:Q 693:= 690:0 672:Q 668:A 664:A 646:A 642:r 638:V 630:A 626:F 617:o 614:A 610:F 606:= 603:0 584:A 582:ν 573:A 571:r 561:A 559:v 554:A 549:A 547:F 542:A 535:F 514:A 510:r 504:A 496:V 493:+ 488:A 484:F 475:o 472:A 468:F 464:= 458:t 455:d 448:A 444:N 440:d 413:] 410:A 399:[ 396:+ 393:] 382:A 379:[ 373:] 362:A 359:[ 356:= 353:] 350:A 339:[ 328:: 326:V 322:A 317:A 315:N 308:V 304:A 302:C 297:A 295:N 289:A 281:A 279:ν 277:( 268:k 258:n 249:A 247:C 243:k 238:A 232:r 230:( 213:A 208:A 206:N 190:) 185:0 182:= 176:t 173:d 166:A 162:N 158:d 150:( 124:V 120:A 66:( 58:( 42:( 20:)

Index

Continuous stirred tank reactor

chemical reactor
chemical engineering
environmental engineering
slurries
perfect mixing
plug flow reactor

steady state
density
n-order reaction
isothermal
reaction
stoichiometric coefficient
Residence time
order of the reaction
Arrhenius temperature dependence

residence time distribution

plug flow reactors


fractional conversion
first order reaction
PFR
space time
rate of reaction
isothermal

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