Spray flash dryer and surfactant solvent removal system
A flash dryer and ejector technology, which is applied in the field of surfactant removal technology, can solve the problems of high risk and explosive mixtures, and achieve high safety effects
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Embodiment 1
[0022] like figure 2 Shown: a jet flash dryer, comprising a jet cylinder, an upper head 71 is fixed on the upper end of the jet cylinder, and a feed port 70 is provided on the upper head 71; A distribution plate 72, a first injector 73, a second distribution plate 74 and a second injector 75; the upper head 71 and the first injector 73 are connected by flanges, and the first distribution plate 72 is sandwiched between the two between. The first injector 73 and the second injector 75 are connected by flanges, and the second distribution plate 74 is sandwiched therebetween. The first distribution plate and the second distribution plate are respectively provided with small holes; the first injector and the second injector are respectively provided with injection pipes 731, and the injection pipes are provided with air intake holes 732; The lower end of the spray cylinder is connected to the gas-solid separation tank 79 through a flange.
[0023] In the jet flash dryer 7, 70% ...
Embodiment 2
[0026] like figure 1 As shown, a solvent removal system for surfactants includes the aforementioned jet flash dryer 7, and also includes a neutralization system 1, a feed pump 2, a preheater 3, a thermal circulation pump 4 and a discharge extruder 8; The discharge port of the neutralization system 1 is connected to the lower feed port of the preheater 3 through the feed pump 2; The lower feed port of the preheater 3 is provided with a check valve 5 on the pipeline; the other way is connected to the feed port 70 of the jet flash dryer 7, and the pipeline is provided with a back pressure valve 6; the injection The lower end of the flash dryer 7 is connected to the discharge extruder 8 .
[0027] The sulfonated acid ester, liquid caustic soda and solvent react in the neutralization system 1 to obtain high-concentration monomers. The materials in the neutralization system are transported by the feed pump 2 and mixed with the hot material transported by the circulating pump 4, and...
Embodiment 3
[0038] A solvent removal system as described in Example 2 was used.
[0039] MESA ester, liquid caustic soda and methanol generate 65% hexadecyl octadecyl fatty acid methyl ester sulfonate in neutralization system 1, the temperature is about 50 °C, and the materials at 130 °C are transported and circulated by feed pump 2 and mixed into the pre-treatment system. Heater 3 is heated, the temperature after heating is 130°C, and the back pressure is 0.9MPa. The circulation ratio is 5:1, that is, the flow rate in the preheater is increased by 5 times.
[0040] The preheated monomer material is transported to the jet flash dryer 7, and the pressure at the feed port drops to 0.4 MPa. Then it enters the injection pipe in the first injector 73 through the small holes on the upper head and the first distribution plate 72, and the temperature will drop. Then, it is sent to the injection pipe in the second injector 75 through the small holes on the second distribution plate 74, the outle...
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