Patent ID: 8080139

Claim:
A method of anhydrous ethanol production using internal circulation by alternation of multiple towers comprising the steps of: i) allowing a 70-99 wt % ethanol aqueous solution, as raw material, to pass a heat interchanger and then enter a vaporizer for heating and vaporizing by steam to obtain a vapor stream of raw material, and then heating the vapor stream of raw material to 80-220° C.; ii) allowing the heated vapor stream of raw material to alternatively enter several adsorption towers which are at adsorption mode in turn from the top thereof for adsorption and dehydration, wherein the pressure of the adsorption towers is 0.1-2.5 MPa and the adsorption process lasts 50-500 seconds; when water concentrations in any one of the adsorption towers is nearly saturated, the feeding of the adsorption tower is stopped; allowing an ethanol stream to flow out from the bottom of the adsorption tower and enter the heat interchanger to heat raw ethanol, and after cooling down by a product cooler, sampling an ethanol product, and entering a qualified product containing 99.5-99.99 wt % ethanol into a product storage tank, sending an unqualified product to a raw ethanol tank for re-processing; iii) after adsorption and dehydration, regulating a valve to allow the remaining alcohol in the tower in which adsorption has been finished to gradually flow into the towers at adsorption mode, until their pressures are equal, establishing internal circulation, which is the course of balancing the pressure in the tower in which adsorption has been finished and the towers in adsorption mode; iv) after internal circulation and pressure balancing, communicating a top portion of the adsorption tower in which adsorption has been finished with a vacuum system to suck out remaining ethanol stream, which is liquefied after mixing with ejecting recycling liquid and becomes a new recycling liquid to be sent to a recycle pump, sending part of the recycling liquid to a rectifying tower and collecting in the raw ethanol tank as raw material after rectification, wherein the liquid in a bottom portion of the rectifying tower is pollution-free waste water, which can be discharged directly, and entering the remaining recycling liquid into an ejector again as ejecting liquid; v) flowing alcohol from an adsorption tower which is in the state of adsorption through a molecular sieve in a vacuum tower from the top to regenerate the molecular sieve after desorption; vi) concentrating the tower after regeneration in which the pressure is −0.01-0.1 MPa to another adsorption tower in which adsorption has been completed, to form an internal circulation, and increasing the pressure and performing a second operation process.