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Energy optimization of ammonia synthesis processes based on oxygen purity under different purification technologies

机译:不同净化技术下基于氧气纯度的氨合成工艺的能量优化

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The energy consumption of an ammonia process plays an important role in the industrial energy consumption. For an ammonia synthesis process using pure oxygen gasification, the energy consumption of cryogenic air separation occupies a large proportion. The purity of the oxygen product from the air separation unit is mostly 99.6% in an ammonia process with pure oxygen gasification. The energy consumption of air separation will decrease significantly, if the purity of the oxygen product is reduced properly, which will lead to the decrease of the energy consumption of the total ammonia process, as the nitrogen element is needed for ammonia synthesis. However, the operating costs of the subsequent units will increase because of the increase of the syngas flow rate. So, there is an optimal oxygen purity that can minimize the energy consumption of the whole ammonia synthesis process. According to temperature, purification technology can be divided into cold and hot technologies. In this work, two different process models for ammonia production from coal with different purification technologies are developed to determine the process energy consumption with different inlet oxygen purity. In the process of ammonia production from coal with cold purification, the reduction of oxygen purity leads to the increase of energy consumption of oxygen compressor, methanol regeneration and refrigeration, and the decrease of nitrogen compressor power consumption. In the process with hot purification, the reduction of oxygen purity leads to the increase of energy consumption of oxygen compressor, preheating and MDEA regeneration, and the decrease of nitrogen compressor power consumption. The relationships between the eight kinds of energy consumption and oxygen purity are linear. Combined with the relationship between oxygen purity and the energy consumption of the air separation unit, the optimal oxygen purity which minimizes the process energy consumption is obtained. In the ammonia production process with cold purification, the optimal oxygen purity is 95%, which can save 10.3% of the energy consumption of the air separation compared with the current process using the 99.6% purity oxygen. While in the ammonia production process with hot purification, the optimal oxygen purity is 96%, which can save 8.4% of the energy consumption of the air separation. (C) 2019 Elsevier Ltd. All rights reserved.
机译:氨法的能耗在工业能耗中起着重要的作用。对于使用纯氧气气化的氨合成工艺,低温空气分离的能耗占很大比例。在纯氧气气化的氨法中,来自空气分离装置的氧气产品的纯度大部分为99.6%。如果适当降低氧气产品的纯度,空气分离的能耗将大大降低,这将导致总氨工艺能耗的降低,因为合成氨需要使用氮元素。然而,由于合成气流量的增加,后续单元的运行成本将增加。因此,存在最佳的氧气纯度,可以使整个氨合成过程的能耗降至最低。根据温度,净化技术可分为冷热技术。在这项工作中,开发了两种使用不同纯化技术从煤中生产氨的不同过程模型,以确定具有不同入口氧气纯度的过程能耗。在通过冷提纯从煤生产氨的过程中,氧气纯度的降低导致氧气压缩机能耗的增加,甲醇的再生和制冷,以及氮气压缩机能耗的降低。在热纯化过程中,氧气纯度的降低导致氧气压缩机能耗,预热和MDEA再生的增加,以及氮气压缩机能耗的减少。八种能量消耗与氧气纯度之间的关系是线性的。结合氧气纯度和空气分离装置能耗之间的关系,可以获得使过程能耗最小化的最佳氧气纯度。在采用冷纯化的氨生产工艺中,最佳氧气纯度为95%,与当前使用99.6%纯度氧气的工艺相比,可以节省空气分离能耗的10.3%。在热纯化制氨过程中,最佳氧气纯度为96%,可节省空气分离能耗的8.4%。 (C)2019 Elsevier Ltd.保留所有权利。

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