Reading task for the first lesson
1. Mass transfer
There are too many factors which influence on technological process. Diffusivity and mass transfer coefficient estimation and common flux equations, although material balance are also presented in typical coordinate systems to permit a wide range of problems to be formulated and solved.
Mass-transfer calculation involve transport properties, such as diffusivities, and other empirical factors that have been found to relate mass-transfer rates to measured “driving forces” in myriad geometries and conditions. The context of the problem dictates whether the fundamental or more applied coefficient should be used. One key distinction is that, whenever there is flow parallel to an interface through which mass-transfer occurs, the relevant coefficient is an empirical combination of properties and conditions. Conversely, when diffusion occurs in stagnant media or in creeping flow without transverse velocity gradient, ordinary diffusivities may be suitable for solving the problem. In either case, it is strongly suggested to employ data, whenever available, instead or relying on correlations.
Figure 1. Flowchart illustrating problem solving approach using mass-transfer rate expression in the context of mass conservation
Most, if not all, problems or applications that involve mass transfer can be
approached by a systematic course of action. In the simplest cases the unknown quantities are obvious. In more complex (e.g., multicomponent, multiphase,

multidimensional, nonisothermal and/or transient) systems, it is more subtle to resolve the known and unknown quantities. For example, in multicomponent systems, one must know the fluxes on the component before predicting their effective diffusivities and vice versa. Figure 1 is a flowchart that illustrates the primary types of information and their relationships, and it applies to many masstransfer problems.
2. Heat transfer
Heat transfer is a discipline of thermal engineering that concerns the exchange of thermal energy from one physical system to another. Heat transfer is classified into various mechanisms, such as heat conduction, convection, thermal radiation, and phase-change transfer. All forms of heat transfer may occur in some systems
(for example, in transparent fluids like the Earth's atmosphere) at the same time.
Heat transfer only occurs because of a temperature-difference driving force and heat flows from the high to the low temperature region.
Heat conduction, also called diffusion, is the direct microscopic exchange of kinetic energy of particles through the boundary between two systems. When an object is at a different temperature from another body or its surroundings, heat flows so that the body and the surroundings reach the same temperature at thermal equilibrium. Conduction happens in gases, liquids and solids. A good example of heat conduction is an ice water bath, where you put ice into water and the whole system stays at a constant equilibrium temperature as long as there is ice present in the water.
Heat convection occurs when bulk flow of a fluid (gas or liquid) carries heat along with the flow of matter in the fluid. The flow of fluid may be forced by external processes, or sometimes (in gravitational fields) by buoyancy forces caused when thermal energy expands the fluid (for example in a fire plume), thus influencing its own transfer. The latter process is sometimes called "natural convection". All convective processes also move heat partly by diffusion, as well. Another form of convection is forced convection. In this case the fluid is forced to flow by use of a pump, fan or other mechanical means.
The final major form of heat transfer is by radiation, which occurs in any transparent medium (solid or fluid) but may also even occur across vacuum (as when the Sun heats the Earth). Radiation is the transfer of energy through space by means of electromagnetic waves in much the same way as electromagnetic

light waves transfer light. The same laws that govern the transfer of light govern the radiant transfer of heat.
3. Chemical Reactors
In chemical engineering, chemical reactors are vessels designed to contain chemical reactions. The design of a chemical reactor deals with multiple aspects of chemical engineering. Chemical engineers design reactors to maximize net present value for the given reaction. Designers ensure that the reaction proceeds with the highest efficiency towards the desired output product, producing the highest yield of product while requiring the least amount of money to purchase and operate. Normal operating expenses include energy input, energy removal, raw material costs, labor, etc. Energy changes can come in the form of heating or cooling, pumping to increase pressure, frictional pressure loss (such as pressure drop across a 90 o elbow or an orifice plate), agitation, etc.
Overview
There are two main basic vessel types:
 tank reactor - a tank
 tubular reactor - a pipe or tube
Both types can be used as continuous reactors or batch reactors. Most commonly, reactors are run at steady-state, but can also be operated in a transient state.
When a reactor is first brought back into operation (after maintenance or inoperation) it would be considered to be in a transient state, where key process variables change with time. Both types of reactors may also accommodate one or more solids (reagents, catalyst, or inert materials), but the reagents and products are typically liquids and gases.
There are three main basic models used to estimate the most important process variables of different chemical reactors:
 batch reactor model (batch),
 continuous stirred-tank reactor model (CSTR), and
 plug flow reactor model (PFR).
Furthermore, catalytic reactors require separate treatment, whether they are batch, CST or PF reactors, as the many assumptions of the simpler models are not valid.
Key process variables include:
 residence time (τ, lower case Greek tau)

 volume (V)
 temperature (T)
 pressure (P)
 concentrations of chemical species (C1, C2, C3, ... Cn)
 heat transfer coefficients (h, U)
Types
CSTR (Continuous Stirred-Tank Reactor)
In a CSTR, one or more fluid reagents are introduced into a tank reactor equipped with an impeller while the reactor effluent is removed. The impeller stirs the reagents to ensure proper mixing. Simply dividing the volume of the tank by the average volumetric flow rate through the tank gives the residence time, or the average amount of time a discrete quantity of reagent spends inside the tank.
Using chemical kinetics, the reaction's expected percent completion can be calculated. Some important aspects of the CSTR:
At steady-state, the flow rate in must equal the mass flow rate out, otherwise the tank will overflow or go empty (transient state). While the reactor is in a transient state the model equation must be derived from the differential mass and energy balances.
All calculations performed with CSTRs assume perfect mixing.
The reaction proceeds at the reaction rate associated with the final (output) concentration.
Often, it is economically beneficial to operate several CSTRs in series or in parallel.
This allows, for example, the first CSTR to operate at a higher reagent concentration and therefore a higher reaction rate. In these cases, the sizes of the reactors may be varied in order to minimize the total capital investment required to implement the process.
It can be seen that an infinite number of infinitely small CSTRs operating in series would be equivalent to a PFR.
PFR (Plug Flow Reactor)
In a PFR, one or more fluid reagents are pumped through a pipe or tube. The chemical reaction proceeds as the reagents travel through the PFR. In this type of reactor, the reaction rate is a gradient; at the inlet to the PFR the rate is very high, but as the concentrations of the reagents decrease and the concentration of the product(s) increases the reaction rate slows. Some important aspects of the PFR:

All calculations performed with PFRs assume no upstream or downstream mixing, as implied by the term "plug flow".
Reagents may be introduced into the PFR at locations in the reactor other than the inlet. In this way, a higher efficiency may be obtained, or the size and cost of the PFR may be reduced.
A PFR typically has a higher efficiency than a CSTR of the same volume. That is, given the same space-time, a reaction will proceed to a higher percentage completion in a PFR than in a CSTR.
For most chemical reactions, it is impossible for the reaction to proceed to 100% completion. The rate of reaction decreases as the percent completion increases until the point where the system reachs dynamic equilibrium (no net reaction, or change in chemical species occurs). The equilibrium point for most systems is less than 100% complete. For this reason a separation process, such as distillation, often follows a chemical reactor in order to separate any remaining reagents or byproducts from the desired product. These reagents may sometimes be reused at the beginning of the process, such as in the Haber process.
Semi-batch reactor
A semi-batch reactor is operated with both continuous and batch inputs and outputs. A fermentor, for example, is loaded with a batch, which constantly produces carbon dioxide, which has to be removed continuously. Analogously, driving a reaction of gas with a liquid is usually difficult, since the gas bubbles off.
Therefore, a continuous feed of gas is injected into the batch of a liquid. An example of such a reaction is chlorination.
Catalytic reactor
Although catalytic reactors are often implemented as plug flow reactors, their analysis requires more complicated treatment. The rate of a catalytic reaction is proportional to the amount of catalyst the reagents contact. With a solid phase catalyst and fluid phase reagents, this is proportional to the exposed area, efficiency of diffusion of reagents in and products out, and turbulent mixing or lack thereof. The assumption of perfect mixing cannot be assumed.