Heat pump rectification device and method for removing sulfide in MTBE
A heat pump rectification and sulfide technology, applied in fractionation, chemical industry, organic chemistry, etc., can solve the problems of unreasonable energy utilization, high energy consumption of desulfurization, failure to achieve energy saving, etc., to improve heat utilization efficiency, simple system, The effect of reducing consumption
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Embodiment 1
[0029] Example 1, MTBE comes from a refinery catalytic reaction rectification unit, characterized by MTBE99.05%, methanol 0.0123%, tert-butanol 0.0324%, methyl sec-butyl ether 0.51%, water 0.00438%, trimethyl- 2-pentene 0.285%, diisobutene 0.0285%, 2-methyl-1-butene 0.0372%, isopentane 0.0399%, dimethyl disulfide 0.0247%, ethyl methyl disulfide 0.0149%, methyl 0.0051% tert-butyl sulfide, 0.00175% diethyl disulfide, 0.00325% dimethyl sulfide, and a total sulfur content of 497ppm. The packing of the rectification tower is wire mesh corrugated structured packing, the number of theoretical plates of the rectification tower is 20, the working pressure of the rectification tower is normal pressure, the feed position is 14 theoretical plates, the reflux ratio is 1.6, the bypass control valve is closed, and the gas at the top of the tower is compressed Afterwards, the pressure is 1.8 bar, and the outlet temperature of the compressor is 73.6°C. The raw material enters the rectificatio...
Embodiment 2
[0030] Example 2, the overall process is the same as Example 1, but the difference is: the total sulfur content is 4188ppm, the sulfur-containing species is dimethyl disulfide 0.1878%, ethyl methyl disulfide 0.1249%, methyl tert-butyl sulfide 0.0851%, diethyl disulfide 0.01125%, dimethyl sulfide 0.00975%. MTBE with a purity of 98.95% enters the device as the raw material. During the rectification and desulfurization process, the number of theoretical plates in the rectification column is 20, the working pressure of the rectification column is normal pressure, the feed position is 14 theoretical plates, the reflux ratio is 2, and the bypass control The valve is closed, the pressure of the tower top gas is 2 bar after being compressed, and the outlet temperature of the compressor is 77.4°C. The raw material enters the rectification column at 1250kg / hr. After the device is in stable operation, the heat load of the main heat exchanger at the bottom of the tower is 0.284Gcal / h, the...
Embodiment 3
[0031] Embodiment 3, the overall process of this embodiment is the same as that of 1. This embodiment simulates the special working condition of insufficient system energy, opens the bypass control valve, bypasses the auxiliary cooler, and the total sulfur content is 110ppm. Among them, dimethyl disulfide 0.0057%, ethyl methyl disulfide 0.0039%, methyl tert-butyl sulfide 0.0009%, diethyl disulfide 0.0005%, dimethyl sulfide 0.0004%, total sulfur The content is 497ppm. MTBE with a purity of 99.2% enters the device as a raw material. During the rectification and desulfurization process, the number of theoretical plates in the rectification tower is 20, the working pressure of the rectification tower is normal pressure, 14 theoretical plates in the feeding position, and the reflux ratio is 1. After the top gas is compressed, its pressure is 1.8 bar, and the outlet temperature of the compressor is 73.6°C. The raw material enters the rectification column at 1250kg / hr. After the dev...
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