Jaenuri, Abdul Rahman Khadafi (2024) Pabrik Asam Salisilat Berbahan Baku Fenol Dengan Proses Kolbe - Schmitt. Undergraduate thesis, UPN Veteran Jawa Timur.
|
Text (Cover)
18031010216-cover.pdf Download (1MB) | Preview |
|
|
Text (BAB 1)
18031010216-bab1.pdf Download (71kB) | Preview |
|
|
Text (BAB 2)
18031010216-bab2.pdf Download (71kB) | Preview |
|
Text (BAB 3)
18031010216-bab3.pdf Restricted to Registered users only until 11 January 2027. Download (73kB) |
||
Text (BAB 4)
18031010216-bab4.pdf Restricted to Registered users only until 11 January 2027. Download (733kB) |
||
Text (BAB 5)
18031010216-bab5.pdf Restricted to Registered users only until 11 January 2027. Download (112kB) |
||
Text (BAB 6)
18031010216-bab6.pdf Restricted to Registered users only until 11 January 2027. Download (45kB) |
||
Text (BAB 7)
18031010216-bab7.pdf Restricted to Registered users only until 11 January 2027. Download (730kB) |
||
Text (BAB 8)
18031010216-bab8.pdf Restricted to Registered users only until 11 January 2027. Download (93kB) |
||
Text (BAB 9)
18031010216-bab9.pdf Restricted to Registered users only until 11 January 2027. Download (132kB) |
||
Text (BAB 10)
18031010216-bab10.pdf Restricted to Registered users only until 11 January 2027. Download (57kB) |
||
Text (BAB 11)
18031010216-bab11.pdf Restricted to Registered users only until 11 January 2027. Download (345kB) |
||
|
Text (DAFTAR PUSTAKA)
18031010216-daftarpustaka.pdf Download (333kB) | Preview |
|
Text (LAMPIRAN)
18031010216-lampiran.pdf Restricted to Registered users only until 11 January 2027. Download (1MB) |
||
|
Text (FLOWSHEET)
18031010216-flowsheet.pdf Download (142kB) | Preview |
Abstract
The planning for the Salicylic Acid factory made from phenol using the Kolbe – Schmitt process is planned for a production capacity of 40,000 tons/year. Briefly, the process description of the Salicylic Acid factory made from phenol using the Kolbe - Schmitt process is as follows: The process of making salicylic acid includes three stages, namely the formation of sodium phenolate, sodium salicylate and salicylic acid. At the stage of sodium phenolate formation, the phenol is reacted with a sodium hydroxide solution using a stirred tank reactor where the two raw materials, namely sodium hydroxide and phenol, are obtained from the supplier. After sodium phenolate is formed, it will then flow to the bubble reactor to be reacted with carbon dioxide, thus forming sodium salicylate. Next, it flows to the decolorization tank. The decoloration process is carried out to remove the yellow color from sodium salicylate by adding activated carbon. After that, the solution is pumped to a filter press to separate the activated carbon cake from the sodium salicylate solution. The filtrate is collected in the filtrate tank, then flowed to the Precipitation Tank for acidification. 66% Sulfuric Acid. The salicylic acid formed will precipitate in the sodium sulfate solution. Then separate the salicylic acid crystals and sodium sulfate solution using a centrifuge. The pure salicylic acid crystals are then dried with a rotary dryer.
Item Type: | Thesis (Undergraduate) | ||||||||
---|---|---|---|---|---|---|---|---|---|
Contributors: |
|
||||||||
Subjects: | T Technology > TP Chemical technology > TP155 Chemical engineering | ||||||||
Divisions: | Faculty of Engineering > Departement of Chemical Engineering | ||||||||
Depositing User: | Mr. Dafi Jae | ||||||||
Date Deposited: | 12 Jan 2024 03:00 | ||||||||
Last Modified: | 12 Jan 2024 03:00 | ||||||||
URI: | http://repository.upnjatim.ac.id/id/eprint/19745 |
Actions (login required)
View Item |