**1. Introduction**

Distillation Technique is a chief process division extensively used in chemical manufacturing, and the growth of distillation column strategy has involved more and more consideration in the latest ages [1, 2]. Reactive distillation (RD) is a mixture of synthetic reaction and partition simultaneously. Catalytic distillation (CD) is a Reactive distillation process in which chemical reactions happen in a solid catalyst. The blend of the split process with catalytic reactions in a catalytic distillation column has many benefits, for example, improved conversion for stability and expected improvement of item selectivity because of the removal of the yields over in situ partings. In accumulation, the produced heat in the reaction might practice for distillation. Thus, the investment and operative expenses can be reduced [3, 4]. The reactive distillation process has been a part of importance most recent 20 years. The mixture of reaction and separation in a single unit is a substitute to traditional distillation, which incorporates reaction, and division in the number of units consequently expands the investment cost of the plant. The three significant useful areas of the reactive distillation column are:


To feat the likelihood of reactive distillation, procedures have been established for initial process design. Two major methods happen for the group of substitutes for a given reaction-parting problem: mathematical optimization and graphically

based conceptual design methods. Mathematical optimization methods are generally very powerful for generating and evaluating design alternatives [6]. Reactive distillation technology is an encouraging process that can rise reaction change, overcome energy feeding, and recover selectivity and investment yield [7]. In previous years, Reactive distillation was widely inspected due to the projecting benefits, and excessive successes have been gained in positions of dynamic control and development strategy [8–12]. The results of the simulation proved that this novel technology is economical on the process charges and easily controls the purity of the product with the only use of a temperature control loop, which shows the potentials of the heat-integrated reactive distillation methodology. To complete additional energy savings, scientists have focused on the project of DWC to superior distillation structures, for example, reactive divided wall distillation, extractive distillation, or azeotropic distillation [10, 13, 14]. Reactive dividing wall column (RDWC) has newly involved countless importance since it has the rewards of together RD and DWC. A technique for the theoretical strategy of the RDWC created on the smallest vapor stream process planned the rate-based modeling method for RDWC [15]. Therefore, it is necessary to study the Heat integrated reactive distillation performances of reaction systems with different characteristics.

ASPEN PLUS simulation provides the benefits in covering steady-state to dynamic simulation for safety analysis and control process. The physical properties methods are required during the Aspen model, to calculate enthalpy, density viscosity, heat capacity, etc. ASPEN PLUS simulator has been used for physical chemistry, chemical thermodynamics, mass and energy balances, chemical reaction engineering, unit operations, and process design and control. It uses an inbuilt numerical model equation to stabilized the process performance. The perfect showing of thermodynamic properties is mainly significant in the parting of non-ideal mixtures and ASPEN PLUS has big information of retreated factors. Methanol (MeOH) and acetic acid (HAc) are essential raw materials in polyvinyl alcohol plants, and they could produce from Methyl Acetate (MeAc) hydrolysis process. Therefore, this process is considering for heat integration purposes.

#### **1.1 Dividing wall column (DWC)**

The petrochemical and chemical divisions are the major manufacturing power clients, representing generally 10% of overall global energy interest and 7% of worldwide greenhouse gases (GHG) outflows. In the chemical process industry, roughly distillation processes utilize 40% of absolute energy [16]. In the distillation procedure, high temperature is utilized, for example, an isolating means. Heat is provided to the lower section of the reboiler to vanish a fluid saturation at a more temperature and it decreases at less temperature while melting in the condenser at the upper section of the distillation column. Hence, the situation is extremely unproductive in the utilization of power. In the 1970s and 1980s, the start of oil emergencies, the power costs turned into the central point in column rate and made a resolve to discover to decrease the energy requirements of distillation. Subsequently, in the new distillation process, the essential objective is process strategies in distillation systems is that how to cut the power utilization. Different strategies have been used to utilized to make the process of distillation more energy effective and extra economical like divided wall columns (DWC), heat integrated distillation columns (HIDiC), and thermally coupled distillation columns (Petlyuk column).

In **Figure 1**, Wright's patent the divided wall column (DWC) in 1949. DWC can save both energy requirements and economic expenses related to conventional distillations. The energy utilization decreases about 20–30% associate with another conventional distillation column [17, 18].

*Heat Integration of Reactive Divided Wall Distillation Column DOI: http://dx.doi.org/10.5772/intechopen.100811*

**Figure 1.** *Divided wall column.*

The Divided wall column contains more than two distinctive split process units into single and more than one vertical section in the middle area. Dividing walls also differentiate a single column into two sections: a pre-fractionator area and the main column. It also used the condenser and reboiler at the top and bottom respectively [19].

Advantages and disadvantages of divided wall columns


A divided wall column might be offered the potential for decreasing both economic and energy prices, the dividing wall columns have main disadvantages. They are:


#### **1.2 Reactive distillation column (RDC)**

Many numerical problems arise in the modeling, design, and optimization of the RDC, which results in simpler and intensified processes with fewer recycle streams, and decreasing waste handling reflects lower investments and operating costs. RDC offers an advanced reaction rate and selectivity; stops the performance of azeotrope, less energy intake, and solvent treatment. Despite all these benefits, the RDC has partial commercial applications; it is because of the control performance and the complexity in the operation of the RDC. For modeling, we have supposed that it operates in adiabatic conditions with the liquid phase. There is no vapor hold-up

**Figure 2.** *Reactive distillation column.*

in any stage of the distillation column (DC). No hydrodynamic effects have been considered escaping the modeling difficulties [20]. **Figure 2** is an actual sketch of the reactive distillation column.

#### **1.3 Reactive dividing wall distillation column (RDWC)**

A reactive dividing-wall column (RDWC) incorporates a reactor and a separator in a single distillation column. The multiple products, non-reacting components, or excessive reagents can be isolated in such a column, that reactive systems have. Because of the strong corporation among control loops, control engineers have a provoking position to control RDWC. Up until now, the investigation of reactive distillation in one divided wall column is scant, particularly for the control. The reason for this work is to consolidate the advantages of reactive distillation with DWC to deliver MeAc and afterward examine the design and control of an RDWC with an exceptional focus on the foundation of control structures. Initially, a subjective connection between the process flow sheet and phase equilibria is set up, and then an RDWC flow sheet is set up.

The reactive distillation column (RDC) and dividing wall column (DWC) both are genuine instances of process heat intensification. Uncertainty reactive distillation and DWC have combined, a reactive divided wall column (RDWC) has been produced. RDWC has an extremely integrated arrangement that contains one condenser, one reboiler, reactive zones, a pre-fractionator, and the main column together in a single distillation setup. The synthesis of Methyl Acetate has been chosen as a test reaction for heat integration purposes.

The synthesis of Methyl Acetate and its reverse reaction are given below.

$$\text{Method} + \text{Acetic Acid} \leftrightarrow \text{Methyl Aceate} + \text{Water} \tag{1}$$

In reactive distillation, it is likely to get more conversion by continuously removing the products from the reaction section. Products have been removed from the lower part of a reactive distillation column and isolated into the distillation column. By joining the reactive distillation column and separation column into the single column, which turns into the reactive divided wall column with side product methanol stream, also the residence period of methanol with acetic acid and water in the sump has come to a minimum level.

*Heat Integration of Reactive Divided Wall Distillation Column DOI: http://dx.doi.org/10.5772/intechopen.100811*

It has achieved greater attention in the chemical industry for the separation process and saves both energy and capital cost. The RDWC technology has not been confined up to ternary separation only but it can also carry out azeotropic separations. The feasibility of the RDWC in the industry depends upon the thermodynamic properties, the composition of the stream that has separated, and the product requirements. **Figure 3** shows the actual pictorial diagram of the RDWC. Although, **Figure 4** shows the simulation sheet of the two-column reactive divided wall distillation column.

#### **1.4 Heat integration of reactive dividing wall column**

The main approach to improve the energy efficiency of the distillation system is by providing heat integration technology [21]; vapor recompression (VRC) and internally heat-integrated distillation column (HIDiC) [22] are two popular techniques for the same. The energy demands and expenses are expanding due to joined hazards, global warming, and the improved requirement upon lubricant introduced from electorally insecure quantities of the sphere have caused in the importance of the thermodynamic efficiency of recent engineering progress for

**Figure 4.** *Flowsheet of RDWC.*

**Figure 5.** *Flowsheet of heat integrated reactive dividing wall column.*

improving. Expanding power efficiency in compound routes not individual offers cost-effective profits and turns into the decreasing radiations resultant from the development activity. The distillation technology is maybe the important significant and extensively used removable technique in the world today about 95% of all liquid split in the synthetic production industry used. Regardless of its evident significance, in general, most of the thermodynamic efficiency of a conventional distillation is about 5–20% [23]. The concept of process intensification has presented to the distillation development in 1970 for further development of energy efficiency [24]. Nevertheless, the energy efficiency of RDWC is not constantly high since the entire heat can only be added to the bottom reboiler at the maximum temperature and impassive from the top condenser at the final temperature. The heat integration technology such as VRC the exciting energy intake has been reduced [25, 26]. The conventional VRC and side VRC techniques are combined into one RDWC; to deliver the intensified heat integrated technique of VRC that are associated with the RWDC structure. Into intensified heat integrated structures, the unoriginal VRC has further divided between the top and bottom of the RDWC to improve overheat vapor through the heat flow as greatly as possible, into more temperature, compressed fluid from the downward reboiler has recycled into the adjacent fluid to vaporize in a transitional reboiler (IR) [27]. The fundamental thought of heat integration technology is that the high-temperature route streams that exchanged heat with cold route streams, which affect in financial use of assets. Subsequently, numerous sorts of exploration on heat-integrated distillation column (HIDiC) has been done in the past few years to research its achievability and reasonableness in certifiable applications as shown in **Figure 5**. Distillation columns such as the Petlyuk column, divided-wall column, heat pump assisted column, adiabatic distillation column, ideal HIDiC (i- HIDiC), and many more this investigation has led to the formation of different technology. The HIDiC structure has until not accepted by many industries then later small scale trials are accepted by the New Energy and Industrial Technology Development Organization (NEDO), Japan; a combined organization between NEDO and TERI (The Energy & Resources Institute), India undertakings more projects in the field of process intensification technology at a conference at New Delhi in January 2017 [28]. This tends to an original thought of process integration by joining reactive dividing wall column and ethics of heat integrated distillation column i.e. R-HIDiC that accepted the synthesis of methyl acetate with significantly lesser energy consumption. The mixture of methyl acetate employing a reactive dividing wall column system is the most

effective and main application of process intensification [29]. Nevertheless, the greatly needed attention to decrement the energy feeding and intensification the efficiency of the current reactive dividing wall column has considered in this research.
