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Method for preparing ethyl caproate by continuous esterification

A technology of ethyl hexanoate and esterification, applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of increasing the number of moles of raw material ethanol, unable to directly recycle, unable to achieve full conversion, etc. , to achieve the effect of saving latent heat of vaporization, large operation flexibility, and energy saving

Inactive Publication Date: 2013-06-19
河北科正化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The above process has the following defects: the esterification rate is low, sulfuric acid produces side reactions, it consumes a lot of energy to separate the reaction water into the vapor phase, the evaporated alcohol is not a finished product and cannot be directly recycled, and the waste water produced by neutralization needs to consume more alkali. Equipment production efficiency is low
[0009] These methods all generally go to focus on improving the rate of esterification, and there are following defects in the use process: increase the molar number of raw material ethanol, the rate of esterification is not much higher if it is improved, and the more the amount of recovery is increased the more Larger, the greater the energy consumption, the greater the loss; changing the catalyst can only increase the esterification rate by a few percentage points, but cannot achieve full conversion, and there is still a separation problem; adding water-absorbing agents to dehydrate in the reaction is time-consuming, energy-consuming, and high-cost

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0017] The method for continuously preparing ethyl hexanoate of the present invention comprises the steps of: packing 1.5 cubic meters of strong acid resin in a stainless steel column with a diameter of 600 mm, the lower port is connected to a preheater, and the upper port is connected to a certain plate in the lower part of the ethanol separation tower, The ethanol separation tower is a 500mm diameter oblique hole sieve plate tower with 65 plates, and an evaporator is installed at the bottom of the tower to evaporate water to generate water vapor as a heat source. Mix hexanoic acid and ethanol in the batching tank at a molar ratio of 1:1.3, use a pump to feed, pass through a flow meter with a flow rate of 1 ton per hour, flow through a preheater, raise the temperature to 80°C, and then After entering the strongly acidic resin layer for esterification, it enters the separation tower, and the esterification rate is determined to be 55%. A stratifier is arranged outside one of t...

Embodiment 2

[0019] The difference between the preparation method of this embodiment and that of Example 1 is that the ethanol separation tower is changed into a mixing tower, the plate tower below the ethyl hexanoate outlet is used, and the upper half is a packed tower. The bottom vapor temperature was 102°C.

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PUM

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Abstract

The invention discloses a method for preparing ethyl caproate by continuous esterification, which comprises the following steps of: mixing caproic acid and ethanol in the mol ratio of 1: (1-1.5), then preheating, esterifying by a fixed bed catalyst layer, then entering an ethanol fractionating tower, extracting 95%(V / V) alcohol obtained at the tower top, using the 95%(V / V) alcohol as a mixture and recycling; discharging the caproic acid and water from the tower bottom, separating out the caproic acid and recycling again; and leading out the total liquid phase from the position above a feed opening in the middle of the tower and naturally layering, wherein the upper layer is the water which reflows into the tower, and the lower layer is an ethyl caproate crude product which is extracted and refined separately. The method has the advantages that the method can operate within a wider esterification range without considering the conversion rate of the caproic acid; the unreacted caproic acid is separated from the water, thereby avoiding the defects of influencing the flavor of the ethyl caproate and reducing the yield caused by blackening and coking of the caproic acid due to heating when in conventional production and recovery; a neutralization washing work procedure is saved, and no neutralizing waste water exists; and the production efficiency is high.

Description

technical field [0001] The invention relates to a method for preparing ethyl caproate through continuous esterification, in particular to a method for continuously and efficiently preparing ethyl caproate. Background technique [0002] Ethyl caproate is the main aroma component of Luzhou-flavor liquor, and its content directly affects the quality of liquor. Because the traditional solid-state brewing method produces liquor, its liquor yield is low, and fragrance substance is few. In recent years, the method commonly used in the production process of new-type liquor is: reduce the alcohol content of edible alcohol, add a part of solid-state distilled liquor, and then blend with the essence containing ethyl caproate. This makes ethyl caproate an indispensable raw material for the production of liquor. The annual use of ethyl caproate in the country is more than 5,000 tons. Therefore, to innovate the production method of ethyl caproate, choose a simple, pollution-free, fast an...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C69/24C07C67/08
Inventor 谷长安谷利敏
Owner 河北科正化工有限公司
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