2015
DOI: 10.3811/jjmf.29.296
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Development of Enormous PSA System for the Recovery of Carbon Dioxide from Blast Furnace Gas

Abstract: PSA system for the recovery of carbon dioxide from blast furnace is examined. From the results of bench plant experimental operation, it was revealed that recovery cost of carbon dioxide was below 2,000 yen per ton. Further experimental operation to assure the commercial PSA system is ongoing.

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Cited by 2 publications
(5 citation statements)
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“…The reduction in vacuum pump power consumption is estimated to be achieved by the effect of the increase of the minimum gas desorption pressure from 6 to 10 kPaA observed in Figure 16. The durability of Zeolite 13X adsorbent under the same feed gas condition was already verified by a pilot-scale CO 2 -PSA operation in our previous work [5], and therefore, the superior performance of the larger size adsorbent is expected to gives us a great advantage for a long term operation of CO 2 -PSA.…”
Section: Co 2 -Psa Pilot Testsmentioning
confidence: 52%
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“…The reduction in vacuum pump power consumption is estimated to be achieved by the effect of the increase of the minimum gas desorption pressure from 6 to 10 kPaA observed in Figure 16. The durability of Zeolite 13X adsorbent under the same feed gas condition was already verified by a pilot-scale CO 2 -PSA operation in our previous work [5], and therefore, the superior performance of the larger size adsorbent is expected to gives us a great advantage for a long term operation of CO 2 -PSA.…”
Section: Co 2 -Psa Pilot Testsmentioning
confidence: 52%
“…The volumetric mass transfer coefficient in the outer layer of the pellet K 1 can be estimated by Yoshida's Equation (5), which includes both the Schmidt number Sc and the Reynolds number Re [26]. By definition, the Reynolds number is proportional to the gas velocity u.…”
Section: Discussionmentioning
confidence: 99%
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“…The demonstration of this technology up to TRL6-7 has been carried out during the consecutive EU programmes CACHET, CAESAR, and STEPWISE [14]. A wide range of additional emerging CO 2 capture technologies have been proposed to target gas streams in the iron and steel industries, either as post-combustion or as a top gas recycle concepts (advanced solvents [15], membranes [16], new solid sorbents for Pressure Swing Adsorption and Vacuum Pressure Swing Adsorption (PSA/VPSA) [17], chemical looping and calcium looping [18,19]). All these technologies present issues regarding stability of functional materials, role of impurities, energy consumption, retrofitability and need of rigorous quantitative estimation of cost and overall process efficiencies.…”
Section: Introductionmentioning
confidence: 99%