Crude terephthalic acid mother solution replacing method
A technology for crude terephthalic acid and p-xylene, applied in separation methods, chemical instruments and methods, liquid displacement, etc., can solve problems such as unstable operation, complex equipment structure, low replacement efficiency, etc., and achieve fast settling speed , Simple equipment structure and high replacement efficiency
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Embodiment 1
[0017] according to figure 1 The equipment shown is used in a terephthalic acid plant to conduct experiments with crude terephthalic acid slurry (including 92% acetic acid, 7.7% water and a small amount of oxidation catalyst) as the raw material. refer to figure 1 with 2 , this replacement tower 17 is divided into three sections, wherein the clarification section area 18 is 150 millimeters high and the circular cross-section diameter is 80 millimeters, and the displacement section area 19 is 900 millimeters high and 60 millimeters in diameter, and the clarification section and the displacement section cross-sectional area ratio are 1.78: 1, the tower The area 20 of the solid stockpiling section at the lower part of the body is an inverted conical design, and the height of the cone is 60 mm; a main shaft 8 is installed in the tower, and 10 sieve plates 9 distributed in the area of the replacement section are connected to the shaft, and the spacing between the plates is 90 mm...
Embodiment 2~5
[0022] Repeat Example 1, except that the diameter of the clarification section is changed, that is, the ratio of the cross-sectional area of the clarification section to the replacement section, the number of sieve plates and the spacing between the plates, and the results are listed in Table 1. The experimental results fully meet the requirements of the subsequent hydrorefining section, and the operation is stable.
[0023] Table 1
[0024] Example number
Embodiment 6~7
[0026] Repeat Example 1, the difference is to change the raw slurry feed temperature, pressure, the results are listed in Table 2. The experimental results fully meet the requirements of the subsequent hydrorefining section, and the operation is stable.
[0027] Table 2
[0028] Example number
PUM
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