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Process flow diagram processing units

Although most process simulation programs feature a graphical user interface (GUI) that creates a drawing that resembles a PED, printouts of these drawings are very seldom used as actual process flow diagrams. The unit operations shown in the process simulation usually do not exactly match the unit operations of the process. The simulation may include dummy items that do not physically exist and may omit some equipment that is needed in the plant but is not part of the simulation. [Pg.162]

Refer to the process flow diagram for Unit 600, Allyl Chloride Purification Process, Beaumont, Texas (Figure C ). [Pg.1114]

Trona Purification Processes. Two processes, named the monohydrate and sesquicarbonate according to the crystalline intermediates, are used to produce refined soda ash from trona. Both involve the same unit operations only in different sequences. Most ash is made using the monohydrate process. Eigure 2 shows simplified flow diagrams for each. [Pg.525]

Development of a preliminary layout requires the following information (/) process flow diagrams (2) plot limits (J) process unit rough area... [Pg.69]

Figure 2 shows a general process flow diagram for almost all production of natural sodium sulfate. Glauber s salt can be converted to anhydrous sodium sulfate by simply drying it in rotary kilns. Direct drying forms a fine, undesirable powder, and any impurities in the Glauber s salt become part of the final product. This process is not used in the United States but is used in other countries. [Pg.204]

Fig. 3. Process flow diagram for a continuous falling film SO sulfonation plant, equipped with a sulfur-burning SO converter unit. See text. Fig. 3. Process flow diagram for a continuous falling film SO sulfonation plant, equipped with a sulfur-burning SO converter unit. See text.
Phase I Preassessment. (/) Audit focus and preparation. (2) Identify unit operations and processes. (J) Prepare process flow diagrams. [Pg.226]

Most flow sheets have one or mote recycles, and trial-and-ettot becomes necessary for the calculation of material and energy balances. The calculations in a block sequential simulator ate repeated in this trial-and-ettot process. In the language of numerical analysis, this is known as convergence of the calculations. There ate mathematical techniques for speeding up this trial-and-ettot process, and special hypothetical calculation units called convergence, or recycle, units ate used in calculation flow diagrams that invoke special calculation routines. [Pg.73]

The next step is to connect the individual unit operations in a block diagram, creating a process flow sheet. Figure 1 is an example of a simplified process flow diagram for a pattem-etch process for a printed wiring-board operation. There are... [Pg.362]

The most common application of carbon adsorption in municipal water treatment is in the removal of taste and odor compounds. Figure 12 provides an example of a process flow diagram for a municipal water treatment plant. In this example water is pumped from the river into a flotation unit, which is used for the removal of suspended solids such as algae and particulate matter. Dissolved air is the injected under pressure into the basin. This action creates microbubbles which become attached to the suspended solids, causing them to float. This results in a layer of suspended solids on the surface of the water, which is removed using a mechanical skimming technique. Go back to Chapter 8 if you need to refresh your memory on air flotation systems. [Pg.416]

Figure 5. Process flow diagram of the conversion unit. (Used with permission of Simulation Sciences Inc.)... Figure 5. Process flow diagram of the conversion unit. (Used with permission of Simulation Sciences Inc.)...
Your flow diagram might not look exactly like the one shown for instance you will probably have represented the fermentation step by fermentation, rather than drawing the bioreactor. Nevertheless you should have all toe unit processes and inputs shown above in your own diagram. [Pg.351]

In an information flow diagram, such as that shown in Figure 4.5b, each block represents a calculation module that is, the set of equations that relate the outlet stream component flows to the inlet flows. The basic function of most chemical processing units (unit operations) is to divide the inlet flow of a component between two or more outlet... [Pg.172]

The outlet streams from a unit can feed forward to other units, or backward (recycle). An information flow diagram for a process consisting of three units, with two recycle streams is shown in Figure 4.7. The nomenclature defined in Figure 4.6 is used to show the stream flows. [Pg.173]

The process flow diagram is shown in Figure 4.11. This diagram is simplified and drawn as an information flow diagram in Figure 4.12. Only those process units in which there is a difference in composition between the inlet and outlet streams are shown. The... [Pg.176]

The next thing that is needed is a program that keeps track of all the process and utility streams, and determines the order in which the individual equipment calculations will be performed. This is sometimes referred to as the executive program. The user of this system has merely to put into computer language the flow diagram, which identifies the units (areas of heat exchangers, number of trays in a distillation column) and their interrelations, and to list the operating characteristics of each unit (the pressures, temperatures, exit compositions), the input variables to the plant... [Pg.418]

To avoid these situations, we need to check for the presence of parallel streams in the flow diagram of the process. When this is the case, one of the individual balances is substituted by a combined balance around the units involved. [Pg.57]

The outlined strategy has been applied to the subsystem of Example 4.4 in Chapter 4. The flow diagram, shown in Fig. 4 of Chapter 4, consists of 7 units interconnected by 15 streams. There are 8 measured flowrates and 7 unmeasured ones. The flowrate measurements with their variances are given in Table 3. In Chapter 4 we identified the subset of redundant equations. In this case it is constituted by one equation that contains the five redundant process variables. By applying the data reconciliation procedure to this reduced set of balances, we obtain the estimates of the measured variables, which are also presented in Table 3. [Pg.101]


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