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Languages : en
Pages : 15
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The system is based on the absorption of hydrogen sulfide (H2S) by stannic (tin) oxide. Two sorbents are required, the first sorbent is tin oxide and the second sorbent is a zinc oxide based material (i.e., zinc ferrite or zinc titanate) which is regenerated by air producing SO2. TDA's process carries out a modified Claus reaction to reduce the SO2 from the second sorbent generation to elemental sulfur. In this case the sulfided stannic oxide forms stannous sulfide (SnS) which reduces the SO2. The absorption by SnO2 could remove over 90% of the H2S from typical coal gas streams, but we use zinc ferrite (or zinc titanate), (a) to reduce H2S to less than 20 ppM and (b) as a source of SO2 in regeneration. Due to stoichiometry of regeneration we want to remove half of the H2S by SnO2 and the remainder by the second sorbent. The reactions with stannic oxide minimize the heat released during H2S removal and regeneration. The absorption by SnO2 is slightly endothermic and cools the gas stream by less that 5°F (2.8°C) during absorption. Regeneration with SO2 is exothermic but releases only 11% of the heat that is liberated in regenerating the ZnO. For a nominal 6.5:1 steam to air the regeneration of ZnO increases the temperature by (asymptotically equal to)400°F. The regeneration of SnO2 increases the temperature by less than 50°F (28°C) in the same gas flow.
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Languages : en
Pages : 15
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Book Description
The system is based on the absorption of hydrogen sulfide (H2S) by stannic (tin) oxide. Two sorbents are required, the first sorbent is tin oxide and the second sorbent is a zinc oxide based material (i.e., zinc ferrite or zinc titanate) which is regenerated by air producing SO2. TDA's process carries out a modified Claus reaction to reduce the SO2 from the second sorbent generation to elemental sulfur. In this case the sulfided stannic oxide forms stannous sulfide (SnS) which reduces the SO2. The absorption by SnO2 could remove over 90% of the H2S from typical coal gas streams, but we use zinc ferrite (or zinc titanate), (a) to reduce H2S to less than 20 ppM and (b) as a source of SO2 in regeneration. Due to stoichiometry of regeneration we want to remove half of the H2S by SnO2 and the remainder by the second sorbent. The reactions with stannic oxide minimize the heat released during H2S removal and regeneration. The absorption by SnO2 is slightly endothermic and cools the gas stream by less that 5°F (2.8°C) during absorption. Regeneration with SO2 is exothermic but releases only 11% of the heat that is liberated in regenerating the ZnO. For a nominal 6.5:1 steam to air the regeneration of ZnO increases the temperature by (asymptotically equal to)400°F. The regeneration of SnO2 increases the temperature by less than 50°F (28°C) in the same gas flow.
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Languages : en
Pages :
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A system for high temperature desulfurization of coal-derived gases using regenerable sorbents. One sorbent is stannic oxide (tin oxide, SnO.sub. 2), the other sorbent is a metal oxide or mixed metal oxide such as zinc ferrite (ZnFe.sub. 2 O.sub. 4). Certain otherwise undesirable by-products, including hydrogen sulfide (H.sub. 2 S) and sulfur dioxide (SO.sub. 2) are reused by the system, and elemental sulfur is produced in the regeneration reaction. A system for refabricating the sorbent pellets is also described.
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Languages : en
Pages : 16
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This contract focuses on the development of sorbents and processes for removal of H2S from hot coal gas with the product of sorbent regeneration being elemental sulfur. TDA Research's process uses a regenerable tin(IV) oxide-based (SnO2) sorbent as the first sorbent and zinc ferrite (or zinc titanate) as a second sorbent.
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Category :
Languages : en
Pages : 9
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The objective is to develop and test a regenerable stannic oxide-based sorbent to remove H[sub 2]S from hot coal gases while producing sulfur as the only product. The detailed technical objectives in support of this are: (1) Develop mechanically strong and chemically inert support materials which will retain their properties through multiple absorption regeneration cycles. (2) Develop mathematical models to predict the performance of large-scale systems from benchscale results. (3) Test the durability of the best sorbent/support combinations. (4) Conduct a bench-scale proof of concept test with the best stannic-oxide sorbent. Several approaches are being used to develop long-life sorbents. The investigators have tested sorbents produced by agglomeration, pressing, and extrusion. To date over 50 formulations have been tested, with several showing promise. Table II presents the results on five of these formulations; all of these formulations had surface areas in excess of 2 m[sup 2]/gm. All of the formulations meet the goals for porosity, tin content, and surface area. The crush strength for a 1/8inches dia. by 1/8inches long sorbent is significantly affected by the method of preparing the sorbent.
Author: Mottlene Wang
Publisher:
ISBN:
Category :
Languages : en
Pages : 318
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Author: Glenn E. Johnson
Publisher:
ISBN:
Category : Hydrogen sulfide
Languages : en
Pages : 36
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Author: Jiang Wu
Publisher: Springer
ISBN: 9811068178
Category : Science
Languages : en
Pages : 162
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Book Description
This book provides extensive information on high-temperature H2S removal for integrated gasification combined cycle (IGCC) coarse gas, together with briefly introductions to the concept of clean coal technology, and to the mechanism and kinetics of hot coal gas desulfurizers. Readers will gain a comprehensive understanding of available control methods for high-temperature H2S removal in IGCC coarse gas and how the technology has been adopted by industry. As such, the book offers a unique resource for researchers and engineers in the fields of energy science and technology, environmental science and technology, and chemical engineering.
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Languages : en
Pages :
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ABSTRACT REMOVAL OF HYDROGEN SULFIDE BY REGENERABLE METAL OXIDE SORBENTS Karayýlan, Dilek M.S., Department of Chemical Engineering Supervisor : Prof. Dr. Timur Doðu Co-Supervisor: Prof. Dr. Gülþen Doðu June 2004, 166 pages High-temperature desulfurization of coal-derived fuel gases is an essential process in advanced power generation technologies. It may be accomplished by using metal oxide sorbents. Among the sorbents investigated CuO sorbent has received considerable attention. However, CuO in uncombined form is readily reduced to copper by the H2 and CO contained in fuel gases which lowers the desulfurization efficiency. To improve the performance of CuO-based sorbents, they have been combined with other metal oxides, forming metal oxide sorbents. Sulfidation experiments were carried out at 627 oC using a gas mixture composed of 1 % H2S and 10 % H2 in helium. Sorbent regeneration was carried out in the same reactor on sulfided samples at 700 oC using 6 % O2 in N2. Total flow rate of gas mixture was kept at 100 ml/min in most of the experiments. In this study, Cu-Mn-O, Cu-Mn-V-O and Cu-V-O sorbents were developed by using complexation method. Performance of prepared sorbents were investigated in a fixed-bed quartz microreactor over six sulfidation/regeneration cycles. During six cycles, sulfur retention capacity of Cu-Mn-O decreased slightly from 0.152 to 0.128 (g S)/(g of Sorbent) while some decrease from 0.110 to 0.054 (g S)/(g of Sorbent) was observed with Cu-Mn-V-O. Cu-V-O showed a very good performance in the first sulfidation and excessive thermal sintering in the first regeneration prevented further testing. Sulfur retention capacity of Cu-V-O was calculated as 0.123 (g S)/(g of Sorbent) at the end of the first sulfidation. In addition, SO2 formation in sulfidation experiments was observed only with Cu-V-O sorbent.
Author: Kyung C. Kwon
Publisher:
ISBN:
Category : Chemical engineering
Languages : en
Pages : 10
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Author: Tatang Hernas Soerawidjaja
Publisher:
ISBN:
Category :
Languages : en
Pages : 156
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