Treatment method of butene oxidative dehydrogenation product
A technology of oxidative dehydrogenation and treatment methods, which is applied in the fields of chemical instruments and methods, hydrocarbons, organic chemistry, etc., and can solve problems such as equipment corrosion and easy polymerization of other oxygen-containing compounds, so as to avoid corrosion, reduce waste water, and remove high rate effect
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Embodiment 1
[0026] A 100,000 tons / year butene oxidative dehydrogenation to butadiene plant adopts figure 1 According to the process technology, the flow rate of the oxidative dehydrogenation product of butene is 79000 kg / hour, the temperature is 80° C., and the pressure is 0.1 MPa. The composition is shown in Table 1, and the total amount of organic acid contained therein is 210 ppm. There are 2 adsorption beds, one open and one standby, horizontal container with a diameter of 2500mm and a length of 6000mm. The adsorbent contains 95% of the weight of alumina. After deacidification, the reaction gas enters the compressor. The compressor is a reciprocating compressor, compressed to After 1.0 MPa, it enters the aldehyde washing tower. The aldehyde washing tower is a plate tower with 10 plates. The top of the tower is fed with low-temperature desalted water at a temperature of 5°C. The amount of desalted water is 4 tons per hour. The top gas goes to the subsequent refining system. The aldehyd...
Embodiment 2
[0031] A 100,000 tons / year butene oxidative dehydrogenation to butadiene plant adopts figure 1According to the process technology, the flow rate of the oxidative dehydrogenation product of butene is 79000 kg / hour, the temperature is 80° C., and the pressure is 0.1 MPa. The composition is shown in Table 1, and the total amount of organic acid contained therein is 210 ppm. There are 2 adsorption beds, one open and one standby, horizontal container with a diameter of 2500mm and a length of 6000mm. The adsorbent contains 95% of the weight of alumina. After deacidification, the reaction gas enters the compressor. The compressor is a reciprocating compressor, compressed to After 1.3MPa, it enters the aldehyde washing tower. The aldehyde washing tower is a plate tower with 10 plates. The top of the tower is fed with low-temperature desalted water at a temperature of 5°C. The amount of desalted water is 3 tons / hour, and the top gas goes to the subsequent refining system. The aldehyde ...
Embodiment 3
[0034] A 100,000 tons / year butene oxidative dehydrogenation to butadiene plant adopts figure 1 According to the process technology, the flow rate of the oxidative dehydrogenation product of butene is 79000 kg / hour, the temperature is 80° C., and the pressure is 0.1 MPa. The composition is shown in Table 1, and the total amount of organic acid contained therein is 210 ppm. There are 2 adsorption beds, one open and one standby, horizontal container with a diameter of 2500mm and a length of 6000mm. The adsorbent contains 95% of the weight of alumina. After deacidification, the reaction gas enters the compressor. The compressor is a reciprocating compressor, compressed to After 1.3MPa, it enters the aldehyde washing tower. The aldehyde washing tower is a sieve plate tower with 8 plates. The top of the tower is fed with low-temperature desalted water at a temperature of 5°C. The amount of desalted water is 3 tons / hour, and the top gas goes to the subsequent refining system , The al...
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