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Recovery device and recovery method for ethyl acetate in beta-carotene extraction wastewater

A carotene and ethyl acetate technology, which is applied in the separation/purification of carboxylate, carboxylate preparation, chemical instruments and methods, etc., can solve the problems of low concentration, difficult recovery, and low polarity of ethyl acetate. Achieve the effects of strong adsorption capacity, easy desorption, and large specific area

Active Publication Date: 2022-04-22
BINZHOU JINLANG BIOTECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] Aiming at the technical problems of low polarity, low concentration and difficult recovery of ethyl acetate in β-carotene extraction wastewater, the invention provides a recovery device and recovery method for ethyl acetate in β-carotene extraction wastewater. The invention can effectively Recovery of low-concentration ethyl acetate in wastewater, high recovery rate, low energy consumption, can reduce COD in wastewater, and has good economy

Method used

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  • Recovery device and recovery method for ethyl acetate in beta-carotene extraction wastewater
  • Recovery device and recovery method for ethyl acetate in beta-carotene extraction wastewater
  • Recovery device and recovery method for ethyl acetate in beta-carotene extraction wastewater

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Embodiment 1

[0029] A recovery device for ethyl acetate in waste water extracted by β-carotene, comprising an adsorption column 1, a condenser 2 and a layered tank 3, the inlet of the adsorption column 1 is connected to the waste water inlet pipe, nitrogen gas inlet pipe, The steam inlet pipe, the organic solvent inlet pipe and the washing water inlet pipe are connected, the outlet of the adsorption column 1 is respectively connected with the desorption outlet pipe, the waste water outlet pipe, and the gas outlet pipe through the main outlet pipe, and the other end of the desorption outlet pipe is connected with the condenser 2 inlet Connected, the outlet of the condenser 2 is connected with the inlet of the layered tank 3, and each connecting pipe is provided with a valve.

[0030] The working principle of this recovery device is: washing water, organic solvent, steam, N 2 And waste water can be passed into the adsorption column according to the recovery method, wherein the washing water,...

Embodiment 2

[0032] A kind of β-carotene extraction wastewater, the COD value is 3.12×10 4 mg / L, the waste water is detected by gas chromatography, the results are as follows figure 2 Shown, ethyl acetate content is 0.621% (v / v) in the waste water.

[0033] Use the recovery device of embodiment 1 to reclaim the ethyl acetate of waste water, step is as follows:

[0034] S1. Take 4.07L of macroporous adsorption resin H-01 and wet it with water, stir it evenly and then pack it into a column. The specifications of the adsorption column are H=0.12m, Φ=0.36m;

[0035] S2. Pretreat the adsorption column:

[0036] (1) Wash the resin with 8.14L of water;

[0037] (2) Push out the water with 8.14L ethanol and soak for 24 hours;

[0038] (3) Evacuate the ethanol, completely replace the solvent with water, and wash until the adsorption column has no ethanol smell;

[0039] S3. The β-carotene extraction wastewater is adsorbed on the column, the flow rate is controlled at 0.5BV / h, and the total co...

Embodiment 3

[0044] A kind of β-carotene extraction wastewater, the COD value is 3.12×10 4 mg / L, ethyl acetate content 0.621% (v / v). Use the recovery device of embodiment 1 to reclaim the ethyl acetate of waste water, step is as follows:

[0045] S1. Continue to use the macroporous adsorption resin H-01 analyzed in Example 1, wet it with water, and then stir evenly to pack it into a column. The specifications of the adsorption column are H=0.12m, Φ=0.36m;

[0046] S2. Pretreat the adsorption column:

[0047] (1) Wash the resin with 8.14L of water;

[0048] (2) Push out the water with 8.14L ethanol and soak for 24 hours;

[0049] (3) Evacuate the ethanol, completely replace the solvent with water, and wash until the adsorption column has no ethanol smell;

[0050]S3. The β-carotene extraction wastewater is adsorbed on the column, the control flow rate is 1BV / h, and the total column volume is 20BV. Take the instantaneous outflow sample when the column volume is 10BV, the column volume is...

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Abstract

The invention relates to the technical field of solvent recovery, in particular to a recovery device and a recovery method for ethyl acetate in beta-carotene extraction wastewater. The recovery device comprises an adsorption column, a condenser and a layering tank, an inlet of the adsorption column is communicated with a wastewater inlet pipe, a nitrogen inlet pipe, a steam inlet pipe, an organic solvent inlet pipe and a washing water inlet pipe through main feeding pipes, and an outlet of the adsorption column is communicated with a desorption outlet pipe, a wastewater outlet pipe and a gas outlet pipe through main discharging pipes. The other end of the desorption outlet pipe is communicated with an inlet of the condenser; an outlet of the condenser is communicated with an inlet of the layering tank; the recovery method comprises the following steps: adsorbing ethyl acetate in beta-carotene extraction wastewater by using an adsorption column filled with macroporous adsorption resin H-01, desorbing the adsorbed ethyl acetate by using steam after adsorption, collecting a desorption solution, standing to separate a water phase and a solvent phase, and collecting the solvent phase. The low-concentration ethyl acetate can be effectively recovered, the recovery rate is high, the energy consumption is low, the COD (Chemical Oxygen Demand) in the wastewater can be reduced, and the economical efficiency is good.

Description

technical field [0001] The invention relates to the technical field of solvent recovery, in particular to a recovery device and recovery method for ethyl acetate in β-carotene extraction wastewater. Background technique [0002] β-carotene belongs to the class of carotenoids with the formula C 40 h 56 , are widely used in food, feed, medicine and cosmetic industries. At present, the production of β-carotene mainly includes two ways of extracting natural β-carotene and synthesizing β-carotene. According to different principles, β-carotene can be synthesized by biological or chemical methods. [0003] The production process of β-carotene usually involves the extraction step of β-carotene, and ethyl acetate is one of the main solvents used in this step. Therefore, a small amount of ethyl acetate often remains in the β-carotene extraction wastewater. Due to the low polarity and low concentration of ethyl acetate, it is difficult to recover. At present, distillation tower reco...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/28C07C67/48C07C67/56C07C69/14C02F101/34
CPCC02F1/28C07C67/48C07C67/56C02F2101/34C02F2209/08C02F2303/16C07C69/14
Inventor 陈正杰张斌
Owner BINZHOU JINLANG BIOTECH