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 Encyclopedia of Physical Science and Technology  EN014A-654  July 28, 2001  16:35






               38                                                                            Reactors in Process Engineering


               A. Autoclave                                      C. Bubble Column
                 1. Description                                    1. Description
               The autoclave reactor is a small cylindrical reactor, built  The bubble column is a tower containing primarily liquid
               to withstand high pressures, used to evaluate the kinet-  (>90%) that has a gas or a lighter liquid sparged into the
               ics of high-temperature, high-pressure reactions and the  bottom, allowing bubbles to rise through the column. The
               production of small quantities of specialty chemicals.  column may contain staging, which enhances the mass
               The reactor is typically packed with a supported catalyst,  transfer characteristics of the reactor. In countercurrent
               and reactant is added by injection. Pressure in the system  operation the reactor is particularly attractive for slightly
               is elevated by increasing the temperature of the autoclave.  soluble gases and liquid–liquid systems. With cocurrent
               Additional pressure, if needed, can be obtained with the  flow and a highly baffled column, the reactor has mass
               injection of additional gaseous reactant or an inert.  transfer characteristics similar to those of a static mixer.
                                                                 The reactor may sometimes contain a solid suspended in
                 2. Classification                                the liquid phase.
               The autoclave is usually a heterogeneous batch reactor
               mainly used for high-pressure kinetic studies. The au-  2. Classification
               toclave is typically a solid catalyzed gas–liquid reaction  The bubble column is a typical gas–liquid heterogeneous
               system.                                           reactor with the design also applicable to liquid–liquid
                                                                 systems. The bubbles rise through the liquid in plug flow.
                 3. Applications
                                                                 The liquid is well mixed by the bubbling gas and seldom
               This reactor allows easy data collection for high-  follows plug flow assumptions.
               temperature, high-pressure reaction systems that have dif-
               ficult flow properties. This includes reactants that are solid  3. Applications
               at room temperature or mixtures of solids and liquids. Typ-
                                                                 The bubble column can withstand high gas velocities and
               ical reactions performed in autoclaves are coal liquefac-
                                                                 still maintain high mass transfer coefficients. This column
               tion, petroleum residuals and coal liquids upgrading, and
                                                                 is particularly attractive for reactions that do not require
               high molecular weight hydrogenation experiments.
                                                                 large amounts of gas absorption or require well-mixed
                                                                 liquids.
               B. Blast Furnace                                    There are numerous applications for bubble columns,
                 1. Description                                  for example, gas–liquid columns include the absorption
                                                                 of isobutylene in sulfuric acid, and liquid–liquid columns
               The blast furnace, a vertical shaft kiln, is the oldest in-  are used for nitration of aromatic hydrocarbons.
               dustrial furnace. Reactant enters in the top of the shaft
               and falls down through a preheating section, a calcinating
                                                                 D. Chemostat–Turbidostat
               section, past oil, gas, or pulverized coal burners, through
               a cooling section, with the product ash falling through a  1. Description
               discharge gate.
                                                                 The chemostat is a biological CSTR where the substrate
                                                                 concentration in the tank is maintained constant. The tur-
                 2. Classification
                                                                 bidostat is similar to the chemostat except that the cell
               The blast furnace operates continuously although the in-  mass in the reactor is kept constant. The primary distinc-
               dividual particles see a batch mode of reaction. The actual  tion between the two reactors is the control mechanism
               reaction conditions must be based on the batch reactor  used to maintain continuous operation. A unique feature
               sequence for the particles since complete conversion is  of a biological CSTR is the washout point. When the flow
               desired. This requires control of the mass throughput in  rate is increased so that the microbes can no longer repro-
               the furnace, but primarily it requires accurate temperature  duce fast enough to maintain a population, the microbes
               control. Control of the solids is maintained at the bottom  wash out of the tank, and the reaction ceases. This washout
               discharge port. Gas flow rate is controlled by blowers or  point represents the limits of maximum flow rate for
               by a stack discharge fan.                         operation.

                 3. Applications                                   2. Classification
               Blast furnaces are used for the production of iron from ore  The chemostat is a biological heterogeneous CSTR. The
               and phosphorus from phosphate rock.               microbes are considered a solid phase, and for aerobic
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