Alcohol Recovery Towers: Principles, Applications and High-efficiency Energy-saving Solutions for Industrial Upgrading

Working Principles of Alcohol Recovery Towers Alcohol recovery towers operate on the principle of differential distillation, leveraging the distinct boiling points and relative volatility of alcohol (ethanol, boiling point 78.5℃) and water (boiling point 100℃) to separate and purify alcohol from dilute aqueous solutions. The separation process is a continuous cyclic operation consisting of four core stages: 1. Feed Pretreatment The dilute alcohol-containing feed liquid (e.g., pharmaceutical fermentation broth, food processing wastewater, chemical solvent waste) is preheated to a temperature close to its boiling point via a heat exchanger. This step recovers waste heat from the tower’s top vapor or bottom residue, reducing the energy consumption required for subsequent vaporization. The preheated feed is then introduced into the middle section of the tower, matching the optimal concentration zone to enhance separation efficiency. 2. Vaporization and Fractionation Inside the tower, the feed liquid flows downward, while the bottom reboiler heats the liquid at the tower base to generate vapor. As the vapor rises countercurrently to the descending liquid, intensive mass and heat transfer occur at the interface between the two phases. Since alcohol has a lower boiling poin...

Scraped Surface Evaporators: Principles, Core Advantages and Multi-field Applications

Working Principles of Scraped Surface Evaporators A scraped surface evaporator (SSE) is a specialized thin-film evaporator designed for handling high-viscosity, heat-sensitive, and fouling-prone materials. Its operation relies on the synergistic effect of mechanical scraping and jacketed heating to form a uniform liquid film, enabling efficient heat transfer and rapid evaporation. The working process is divided into four key stages: 1. Feed Introduction The raw material—ranging from viscous pastes to suspensions containing solid particles—is pumped into the evaporator’s cylindrical shell from the top or bottom inlet. The feed rate is precisely controlled to match the scraping speed, ensuring optimal liquid film thickness (typically 0.1–1 mm). 2. Thin-film Formation and Heat Transfer The evaporator’s inner wall is equipped with a heating jacket, where a heat transfer medium (e.g., steam, thermal oil) circulates to provide uniform heating. A rotating shaft with fixed wiper blades (scrapers) rotates at a speed of 50–500 rpm along the inner wall. As the shaft turns, the scrapers continuously spread the incoming feed into a thin, turbulent liquid film across the heated surface. This mechanical action eliminates boundary layer resistance and p...

Extraction Columns: A Comprehensive Guide to Working Principles and Industrial Applications of High-efficiency Separation Equipment

Working Principles of Extraction Columns The core operating principle of extraction columns is liquid-liquid extraction, a separation technology that leverages the difference in solubility of target solutes in two immiscible or partially miscible solvents. One solvent (termed the extractant) has a high affinity for the target solute, while the other (termed the raffinate) is the original carrier phase of the solute. The separation process inside the extraction column involves three key stages: 1. Phase Contact and Mass Transfer The two immiscible liquid phases are introduced into the column from different positions, forming a countercurrent or co-current flow pattern. Countercurrent flow is the dominant mode in industrial applications due to its higher separation efficiency. In this mode, the extractant phase flows upward, and the raffinate phase flows downward (or vice versa). Intensive contact occurs at the interface between the two phases, driving the target solute to diffuse from the raffinate phase to the extractant phase. This mass transfer process continues until the solute reaches a dynamic equilibrium between the two phases. 2. Phase Dispersion and Enhancement To maximize the mass transfer rate, extraction columns are equipped with internal components that dispers...

Principles, Core Structure and Industrial Applications of Distillation Columns

Working Principles of Distillation Columns The operation of distillation columns is fundamentally based on the difference in relative volatility of components within a mixture. Relative volatility, defined as the ratio of vapor pressures of two components at the same temperature, dictates the feasibility and efficiency of separation. The separation process unfolds in three core stages: Feed Preheating and Introduction The raw multi-component mixture is preheated to a temperature close to its boiling point using a dedicated heater. This preheating step minimizes the energy required for vaporization inside the column and facilitates rapid vapor-liquid equilibrium establishment post-feeding. The preheated mixture is then introduced into the middle section of the column through a feed inlet, a position optimized to balance the separation of light and heavy components. Vapor-liquid Contact and Mass Transfer Upon entering the column, the mixture splits into two phases. The liquid phase flows downward along the internal components, while the vapor phase rises upward, driven by continuous heating from the reboiler at the column bottom. During countercurrent contact, intensive heat and mass transfer occur at the vapor-liquid interface: - Low-boiling-point components in th...