Continuous production method for leather fatting agent
A technology of leather fatliquoring agent and production method, which is applied in leather impregnation, chemical treatment of small raw hide/big raw hide/leather skin/fur, small raw hide/large raw hide/leather/fur treatment, etc., and can solve problems affecting the actual application of products Problems such as layering of production products and complex preparation process, etc., to achieve the effect of easy control, difficult control, and easy access to raw materials
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Embodiment 1
[0028] At a temperature of 63±2°C, mix 1300kg of mineral oil solvent, 250kg (where R 1 for-C 12 h 25 , m=2), 250kg (where R 2 for-C 14 h 29 , n=3) two kinds of fatty alcohol polyoxyethylene ether monomers with different carbon chain lengths are added to material mixer 1 continuously and uniformly according to the speed of 300kg / h, 50kg / h and 50kg / h respectively; The homogeneous material flowing out and the liquid maleic anhydride are mixed in the material mixer 2, wherein the total mixing amount of the liquid maleic anhydride is 125kg, and the flow rate continuously injected into the mixer 2 is 25kg / h. The uniformly mixed material from the material mixer 2 is continuously transferred to the parallel stainless steel esterification reaction insulation kettle 3 or 4 with a volume of 1500L (wherein: when the material in the insulation kettle 3 reaches the set liquid level, the interlock device is automatically activated. Switch to the insulation kettle 4), under the prote...
Embodiment 2
[0032] At a temperature of 60±2°C, mix 1200kg of mineral oil solvent, 200kg (where R 1 for-C 14 h 29 , m=3), 300kg (where R 2 for-C 16 h 33, n=4) two kinds of fatty alcohol polyoxyethylene ether monomers with different carbon chain lengths are added to material mixer 1 continuously and uniformly according to the speed of 240kg / h, 40kg / h and 40kg / h respectively; The homogeneous material flowing out and the liquid maleic anhydride are mixed in the material mixer 2, wherein the total mixing amount of the liquid maleic anhydride is 125kg, and the flow rate continuously injected into the mixer 2 is 20kg / h. The uniformly mixed materials from the material mixer 2 are transferred continuously at a constant speed to the parallel enamel material esterification reaction insulation kettle 3 or 4 with a volume of 1000L (wherein: when the material in the insulation kettle 3 reaches the set liquid level, the interlock device is automatically activated Switch to the insulation kettle...
Embodiment 3
[0035] At a temperature of 57±2°C, mix 1500kg of mineral oil solvent, 187.5kg (where R 1 for-C 16 h 33 , m=2), 375kg (where R 2 for-C 18 h 37 , n=3) two kinds of fatty alcohol polyoxyethylene ether monomers with different carbon chain lengths are added to the material mixer 1 continuously and uniformly according to the speed of 250kg / h, 30kg / h and 62kg / h respectively; The homogeneous material flowing out and the liquid maleic anhydride are mixed in the material mixer 2, wherein the total mixing amount of the liquid maleic anhydride is 140kg, and the flow rate continuously injected into the mixer 2 is 25kg / h. The uniformly mixed materials from the material mixer 2 are transferred continuously at a constant speed to the parallel enamel material esterification reaction insulation kettle 3 or 4 with a volume of 1000L (wherein: when the material in the insulation kettle 3 reaches the set liquid level, the interlock device is automatically activated Switch to the insulatio...
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