Process for producing alcohol-ether hydrazine under medium/low-pressure
A production process and low-pressure alcohol technology, which is applied in the field of medium and low-pressure alcohol and ether hydrazine production process, can solve the problems of low methanol synthesis rate, low efficiency of methanol synthesis unit, high energy consumption, etc., and achieve the effect of reducing compression power consumption
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Embodiment 1
[0034] Methanol hydrazine process using coal as raw material.
[0035] refer to figure 1 , the semi-water gas (conventional process) obtained from coal oxygen-enriched oxidation is sent to compression 2 after crude desulfurization, transformation, decarburization 1, and fine desulfurization. The recirculating gas will enter the gas preheater and exchange heat with the hot synthesis gas coming out of the bottom of the synthesis tower. It will be heated to 200-220°C. It will enter the ring gap of the catalyst frame from the bottom of the synthesis tower and radially enter the catalyst between the tubes from the circumferential direction. Layer, at 225-255°C, hydrogen reacts with carbon monoxide and carbon dioxide to produce methanol and water. After the reaction, the gas converges in the central gas collecting pipe (temperature is 230-280°C) and then exits the synthesis tower. The gas enters the shell side of the intermediate heat exchanger and exchanges heat with the gas enter...
Embodiment 2
[0039] Methanol hydrazine with natural gas as raw material.
[0040] refer to figure 2 , the desulfurized natural gas undergoes one-stage steam reforming and two-stage autothermal reforming in the reforming process, then enters "transformation" and "decarbonization 1" to adjust the hydrogen-carbon ratio and then compresses it to 7.0MPa, which is separated from the circulating gas oil The recycle gas will join into the methanol synthesis tower, the methanol synthesis pressure is 6.95MPa and the temperature is 266°C. The tail gas after the synthesis outlet gas is separated from the alcohol product enters the deep shift to convert the CO in it into H 2 and CO 2 , and then remove CO by "decarbonization 2" 2 , enter the PSA CO removal system to remove trace CO, add pure nitrogen from the oxygen production process, adjust the hydrogen-nitrogen ratio of the gas to 3:1, and then combine with the ammonia synthesis cycle gas after oil removal and send it to the ammonia synthesis tow...
Embodiment 3
[0044] This example is the same as Example 1, except that the synthetic methanol part is changed to adopt a fluidized bed process to synthesize dimethyl ether. The dimethyl ether synthesis catalyst used is a copper-based composite catalyst, the reaction temperature is 268° C., and the reaction pressure is 5.0 MPa. Part of the gas after separation of dimethyl ether enters the cycler as a cycle gas, and the other part is sent to the "deep shift" process to convert the CO contained in this part of the tail gas into H 2 and CO 2 , and then into decarburization 2, the contained CO 2 Removal, the residual trace CO in the secondary decarburization gas enters the PSA system and is completely removed. In this way, the purified gas is added with an appropriate amount of pure nitrogen from the nitrogen production process, and the hydrogen-nitrogen ratio of the gas is adjusted to 3, and then synthesized with ammonia. Meet and send to the ammonia synthesis tower, the ammonia synthesis pr...
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