Method for improving degree of exhaustion during wood dyeing
A technology of dyeing rate and wood, which is applied in the field of wood dyeing, can solve the problems of inability to remove acidic substances, unsatisfactory pretreatment effect, and inability to greatly improve supercritical polarity, so as to achieve the effect of increasing polarity and increasing solubility
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Embodiment 1
[0029] A method for improving the dyeing uptake rate of wood reactive dyes of the present invention comprises the following steps:
[0030] (1) Preparation of entrainer: Take acetone, ethanol and N,N-dimethylhexadecylamine, and mix them according to the volume ratio of 60:32:8 to obtain a mixed solution of acetone, ethanol and fatty alkyl tertiary amine, That is entrainer.
[0031] (2) Process the poplar heartwood into a 50×20×5mm four-sided light test piece, adjust it to a moisture content of 80%, and put it in supercritical CO 2 in the extraction cylinder. Put the mixed solution of acetone, ethanol, and N,N-dimethylhexadecylamine into the entrainer tank. CO with a temperature of 35°C and a flow rate of 20L / h 2 The fluid is passed into the extraction cylinder, and at the same time, the mixed solution in the entrainer tank is passed into the extraction cylinder at a flow rate of 15mL / min with a high-pressure pump, until the pressure in the extraction cylinder is 15MPa, and ...
Embodiment 2
[0040] A method for improving the dyeing uptake rate of wood reactive dyes of the present invention comprises the following steps:
[0041] (1) Preparation of entrainer: take acetone, ethanol and N,N-dimethyldodecylamine, and mix them according to the volume ratio of 50:40:10 to obtain a mixed solution of acetone, ethanol and fatty alkyl tertiary amine, That is entrainer.
[0042] (2) Process the eucalyptus heartwood into a 50×20×5mm four-sided light test piece, adjust the moisture content to 100%, and put in supercritical CO 2 in the extraction cylinder. Put a mixed solution of acetone, ethanol, and N,N-dimethyldodecylamine into the entrainer tank, and pass through CO at a temperature of 45°C. 2 Fluid, until the pressure in the extraction cylinder is 25MPa, carry out supercritical CO 2 Fluid extraction for 60min. After the extraction is completed, the pressure is quickly released at a rate of 10MPa / min, and the temperature is lowered to recover CO 2 , acetone, ethanol, N...
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