High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge
Biogas desulfurization can be performed by adsorption, although new materials are needed since commercial adsorbents are expensive. In this regard, three types of sewage-sludge were studied as precursors to obtain low-cost adsorbents in a previous paper, attaining the best precursor from a sewage-sl...
| Authors: | ; |
|---|---|
| Format: | Article |
| Status: | Accepted version |
| Publication date: | 2016 |
| Country: | España |
| Institution: | Universidad de Sevilla (US) |
| Repository: | idUS. Depósito de Investigación de la Universidad de Sevilla |
| OAI Identifier: | oai:idus.us.es:11441/172610 |
| Online Access: | https://hdl.handle.net/11441/172610 https://doi.org/10.1016/j.fuproc.2016.01.036 |
| Access Level: | Open access |
| Keyword: | Regeneration Adsorption Low-cost adsorbents Hydrogen sulfide Biogas Desulfurization |
| _version_ | 1878742027157372928 |
|---|---|
| author | González Aguilera, Paloma |
| author2 | Gutiérrez Ortiz, Francisco Javier |
| author2_role | author |
| author_browse | González Aguilera, Paloma Gutiérrez Ortiz, Francisco Javier |
| author_facet | González Aguilera, Paloma Gutiérrez Ortiz, Francisco Javier |
| author_role | author |
| collection | idUS. Depósito de Investigación de la Universidad de Sevilla |
| description | Biogas desulfurization can be performed by adsorption, although new materials are needed since commercial adsorbents are expensive. In this regard, three types of sewage-sludge were studied as precursors to obtain low-cost adsorbents in a previous paper, attaining the best precursor from a sewage-sludge that was thermally treated up to 700 °C. However, it must be regenerated to make the process feasible. To find an economical and environmentally friendly regeneration process, an experimental design was performed aimed at minimizing the use of resources such as water consumption, time and the temperature required while achieving a high rate of regeneration. The selected in-situ regeneration consists of entering firstly steam at relatively low temperature (< 250 °C), against most of published studies, followed by a second step with air. Besides, it can be performed in only 20 min, giving a large feasibility to the overall continuous adsorption process, with very low energy cost and duration for the regeneration. As a relevant result, the thermally treated sewage-sludge was regenerated up to 14 times, and although the adsorption capacity decreased 2.7% on average in each adsorption/regeneration cycle, the cost relative to the adsorbent may be reduced to 20% of the cost of using fresh adsorbent. |
| eu_rights_str_mv | openAccess |
| format | article |
| id | ES_eefa4bebba019e12eda3fc6f4eeffdf7 |
| institution | Universidad de Sevilla (US) |
| instname_str | Universidad de Sevilla (US) |
| network_acronym_str | ES |
| network_name_str | España |
| oai_identifier_str | oai:idus.us.es:11441/172610 |
| publishDate | 2016 |
| publishDateSort | 2016 |
| publisher | Elsevier |
| publisherStr | Elsevier |
| reponame_str | idUS. Depósito de Investigación de la Universidad de Sevilla |
| spelling | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge González Aguilera, Paloma Gutiérrez Ortiz, Francisco Javier Regeneration Adsorption Low-cost adsorbents Hydrogen sulfide Biogas Desulfurization Biogas desulfurization can be performed by adsorption, although new materials are needed since commercial adsorbents are expensive. In this regard, three types of sewage-sludge were studied as precursors to obtain low-cost adsorbents in a previous paper, attaining the best precursor from a sewage-sludge that was thermally treated up to 700 °C. However, it must be regenerated to make the process feasible. To find an economical and environmentally friendly regeneration process, an experimental design was performed aimed at minimizing the use of resources such as water consumption, time and the temperature required while achieving a high rate of regeneration. The selected in-situ regeneration consists of entering firstly steam at relatively low temperature (< 250 °C), against most of published studies, followed by a second step with air. Besides, it can be performed in only 20 min, giving a large feasibility to the overall continuous adsorption process, with very low energy cost and duration for the regeneration. As a relevant result, the thermally treated sewage-sludge was regenerated up to 14 times, and although the adsorption capacity decreased 2.7% on average in each adsorption/regeneration cycle, the cost relative to the adsorbent may be reduced to 20% of the cost of using fresh adsorbent. Elsevier https://hdl.handle.net/11441/172610 https://doi.org/10.1016/j.fuproc.2016.01.036 |
| spellingShingle | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge González Aguilera, Paloma Regeneration Adsorption Low-cost adsorbents Hydrogen sulfide Biogas Desulfurization |
| status_str | acceptedVersion |
| title | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| title_full | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| title_fullStr | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| title_full_unstemmed | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| title_short | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| title_sort | High performance regenerative adsorption of hydrogen sulfide from biogas on thermally-treated sewage-sludge |
| topic | Regeneration Adsorption Low-cost adsorbents Hydrogen sulfide Biogas Desulfurization |
| topic_facet | Regeneration Adsorption Low-cost adsorbents Hydrogen sulfide Biogas Desulfurization |
| url | https://hdl.handle.net/11441/172610 https://doi.org/10.1016/j.fuproc.2016.01.036 |