Abstract:Abstract:With the rapid growth in demand for industrial gas in steel and chemical industries, there has been significant emphasis placed on the development of China's large-scale air separation technology. Currently, the maximum capacity of a single unit has been able to attain 120 000 Nm 3 /h (oxygen), and the specific power consumption of 0.38 kWh/m 3 . This paper reviews the current state-of-the-art for large-scale cryogenic air separation systems being deployed in China. A brief introduction to the history… Show more
“…1 Oxygen is used by the steel industry in massive quantities, but it is also an important reactant in the manufacturing of a wide variety of chemicals. 2,3 Moreover, oxygen is a key component of oxy-fuel combustion, which improves efficiency and greatly reduces the NO x pollutants in flue gas. 4,5 Oxy-fuel combustion is also an approach to carbon capture.…”
The
separation of O2 and N2 from air is of
great importance in a variety of industrial contexts, but the primary
means of accomplishing the separation is cryogenic distillation, an
energy-intensive process. A material that could enable air separation
to occur at conventional temperatures would be of great economic and
environmental benefit. Metalated catecholates within metal–organic
frameworks have been considered for other gas separations and are
shown here to have significant potential for air separation. Calculations
of interaction energies between catecholates with first-row transition
metals and guests O2 and N2 were performed using
density functional theory and multireference complete active space
self-consistent field followed by second-order perturbation theory.
A general recipe is offered for active space selection for metalated
catecholate systems. The multireference results are used to rationalize
O2 binding in terms of redox activity with the metalated
catecholate. O2 is predicted to bind more strongly than
N2 for all cases except Cu2+, with general agreement
in the binding trends among all methods.
“…1 Oxygen is used by the steel industry in massive quantities, but it is also an important reactant in the manufacturing of a wide variety of chemicals. 2,3 Moreover, oxygen is a key component of oxy-fuel combustion, which improves efficiency and greatly reduces the NO x pollutants in flue gas. 4,5 Oxy-fuel combustion is also an approach to carbon capture.…”
The
separation of O2 and N2 from air is of
great importance in a variety of industrial contexts, but the primary
means of accomplishing the separation is cryogenic distillation, an
energy-intensive process. A material that could enable air separation
to occur at conventional temperatures would be of great economic and
environmental benefit. Metalated catecholates within metal–organic
frameworks have been considered for other gas separations and are
shown here to have significant potential for air separation. Calculations
of interaction energies between catecholates with first-row transition
metals and guests O2 and N2 were performed using
density functional theory and multireference complete active space
self-consistent field followed by second-order perturbation theory.
A general recipe is offered for active space selection for metalated
catecholate systems. The multireference results are used to rationalize
O2 binding in terms of redox activity with the metalated
catecholate. O2 is predicted to bind more strongly than
N2 for all cases except Cu2+, with general agreement
in the binding trends among all methods.
“…Industrial gases, such as nitrogen, oxygen, and helium, play a crucial role in steel, metallurgical, coal chemical, and other modern industries . The air separation unit (ASU), which produces these industrial gases from atmospheric air by cryogenic distillation, is extensively adopted as the most economical and reliable method to obtain these gases in large-scale gas production . In an ASU, the compressed air (at approximately 0.6 MPa) is fed into an air prepurification system to remove impurities such as CO 2 and H 2 O by temperature swing adsorption (TSA) with zeolite 13X and active aluminum, to prevent the interior of the distillation column from being obstructed by frozen impurities .…”
Section: Introductionmentioning
confidence: 99%
“…1 The air separation unit (ASU), which produces these industrial gases from atmospheric air by cryogenic distillation, is extensively adopted as the most economical and reliable method to obtain these gases in largescale gas production. 2 In an ASU, the compressed air (at approximately 0.6 MPa) is fed into an air prepurification system to remove impurities such as CO 2 and H 2 O by temperature swing adsorption (TSA) with zeolite 13X and active aluminum, to prevent the interior of the distillation column from being obstructed by frozen impurities. 3 Since the volume fraction of CO 2 is 400−1500 ppm in the atmosphere, the partial pressure of CO 2 is lower than 1 kPa in the prepurification system.…”
The current force fields used in grand canonical Monte Carlo (GCMC) simulations are frequently found to underestimate the low-pressure adsorption of CO 2 on zeolite 13X, which is crucial for engineering applications, including air prepurification and carbon capture from air. In this paper, a series of GCMC simulations are performed with a cation-free 13X model to study the influence of the force field parameters for host−guest interaction pairs on low-pressure adsorption. The unique effects of the equilibrium diameters of the interaction pairs on loading under low pressures are studied, and these effects are classified as one of three affecting modes according to their relative value for the interatomic distance of the interaction pair. Based on these results, six possible trends for a low-pressure adsorption isotherm with a changing equilibrium diameter are predicted. By revealing the different affecting modes caused by the microstructure of the host−guest interaction, the particular effects of the interaction pairs are explained. An efficient method to obtain the force field is thus proposed to develop a more accurate force field for lowpressure adsorption. The obtained force field is validated by comparing its results to experimental loading and isosteric heat data from the literature and by performing adsorption experiments in NaX with different Si/Al ratios.
“…Stirling type pulse tube cryocoolers (SPTC), having the benefit of no moving parts at the cold end, could be more reliable and require lower maintenance than Gifford-McMahon (GM) and Stirling cryocoolers (Li et al, 2014;Zhang et al, 2014). However, there are still serious unsolved problems in large scale SPTC.…”
High power pulse tube cryocoolers are expected to be a very promising candidate for high temperature superconductors (HTS) cooling. Unfortunately there are still some problems significantly deteriorating the performance of these cryocoolers, one of which is temperature inhomogeneity. Several different theories have been proposed to explain the mechanism and many factors have been indicated as contributors to the generation and development of temperature inhomogeneity. However, some relations between these factors are seldom noticed, nor classified. The underlying mechanisms are not yet clear. The paper classifies, as internal and external, factors leading to temperature inhomogeneity based on their location. We examine some apparently unreasonable assumptions that have been made and difficulties in simulation and measurement. Theoretical and experimental research on the driving mechanism and suppression of temperature inhomogeneity is reviewed, and potential analysis and measurement methods which could be used in future are identified.
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