Adaptation of an existing O2 stage to Strong Alkaline Treatment (SAT) when iming at production of dissolving-like hardwood pulps (Record no. 1530)
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| 000 -LEADER | |
|---|---|
| fixed length control field | 02760nam a2200301 a 4500 |
| 005 - DATE AND TIME OF LATEST TRANSACTION | |
| control field | 20260817161512.0 |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION | |
| fixed length control field | |
| 035 ## - SYSTEM CONTROL NUMBER | |
| System control number | .b12341678 |
| 100 0# - MAIN ENTRY--PERSONAL NAME | |
| Personal name | Supanee Phiphatwitthaya |
| 245 10 - TITLE STATEMENT | |
| Title | Adaptation of an existing O2 stage to Strong Alkaline Treatment (SAT) when iming at production of dissolving-like hardwood pulps |
| 260 ## - PUBLICATION, DISTRIBUTION, ETC. | |
| Place of publication, distribution, etc. | Pathumthani : |
| Name of publisher, distributor, etc. | Asian Institute of Technology, |
| Date of publication, distribution, etc. | 2013 |
| 300 ## - PHYSICAL DESCRIPTION | |
| Accompanying material | 1 online resource |
| 500 ## - GENERAL NOTE | |
| General note | A thesis submitted in partial fulfillment of the requirements for the degree of Master of Science in Pulp and Paper Technology, School of Environment, Resources and Development |
| 520 ## - SUMMARY, ETC. | |
| Summary, etc. | This Thesis deals with an attempt to produce dissolving-like Eucalyptus Kraft pulps. Instead of using the pre-hydrolyses step, the mill pulp after Kraft Cooking was subjected to a strong alkali treatment (SAT) in which the treatment conditions were widely varied. This step was used instead of O2-delignification. So treated pulps were then D EP D bleached to a brightness level close to 90% ISO. It is shown that it is possible to produce dissolving-like Eucalyptus pulps with high final brightness, suitable pulp viscosity and with interesting dissolving pulp properties (pentosans and alpha-cellulose contents) without pre-hydrolyses of the Kraft pulp. It is further shown that the O2 delignification stage can be converted to hot caustic extraction by substantially increasing the alkalinity in this stage. For the best process-economy, the temperature in the SAT stage should be between 40 and 80oC and the alkali level should be around 400 kg/tp. However for achieving the most suitable quality parameters for the bleached dissolving pulp-like pulps (low enough kappa number i.e. lignin content, low enough pentosan content i.e. hemicelluloses and high enough alpha-cellulose content), the alkalinity in the SAT-step should be increased and higher temperature than 40C should be applied. It is recommended to measure also dissolving pulp{u2019}s filterability (the Kw number) and cellulose reactivity (the Fock{u2019}s number) in order to avoid any unnecessary sub-optimization efforts. |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical term or geographic name entry element | Water |
| General subdivision | Dissolved oxygen |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical term or geographic name entry element | Hardwoods |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Nazhad, Mousa M., |
| Relator term | Chairperson |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Bohez, Erik L.J., |
| Relator term | Examination Committee |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Yakupitiyage, Amararatne, |
| Relator term | Examination Committee |
| 700 1# - ADDED ENTRY--PERSONAL NAME | |
| Personal name | Basta, Jiri, |
| Relator term | Examination committee |
| 710 2# - ADDED ENTRY--CORPORATE NAME | |
| Corporate name or jurisdiction name as entry element | Royal Thai Government, |
| Relator term | Scholarship donor |
| 710 2# - ADDED ENTRY--CORPORATE NAME | |
| Corporate name or jurisdiction name as entry element | AIT Fellowship, |
| Relator term | Scholarship donor |
| 856 ## - ELECTRONIC LOCATION AND ACCESS | |
| Materials specified | Full-Text |
| Uniform Resource Identifier | <a href="http://203.159.5.9/ait-thesis/detail.php?q=B04767">http://203.159.5.9/ait-thesis/detail.php?q=B04767</a> |
| 907 ## - LOCAL DATA ELEMENT G, LDG (RLIN) | |
| a | .b12341678 |
| b | mnait |
| c | j |
| 902 ## - LOCAL DATA ELEMENT B, LDB (RLIN) | |
| a | 240423 |
| 998 ## - LOCAL CONTROL INFORMATION (RLIN) | |
| Operator's initials, OID (RLIN) | 0 |
| Cataloger's initials, CIN (RLIN) | 200108 |
| First date, FD (RLIN) | m |
| -- | a |
| -- | j |
| -- | 0 |
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