Vashti, Revita Arendri (2025) PRA RENCANA PABRIK MONOISOPROPILAMINE DARI DIMETIL KETON DENGAN MENGGUNAKAN PROSES HIDROAMINASI. Undergraduate thesis, UPN Veteran Jawa Timur.
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Abstract
The Monoisopropylamine (C3H9N) factory using dimethyl ketone (CH3COCH3), ammonia (NH3) and hydrogen (H2) as raw materials, which will be established in 2030, is located in Pasirsari, Cikarang, Bekasi, West Java. The ammonia used by the factory as raw material is obtained from PT. Pupuk Kujang in Cikampek, Karawang, West Java with a capacity of 660,000 tons/year with a purity of 99.5%. Dimethyl ketone is also obtained from PT. Anugrah Visi Cemerlang in Pucung, North Bekasi, West Java with a capacity of 100,000 tons/year with a purity of 99%. Hydrogen is obtained from PT. Sulfindo Adiusaha in Mangunreja, Serang, Banten with a capacity of 2,295,453 tons/year with a purity of 100%. This factory uses a continuous operating system for 24 hours a day with 330 working days and 175 employees. The product produced is Monoisopropylamine (C3H9N) with a purity of 99.3%. Monoisopropylamine has many benefits in the industrial sector, for example in the chemical industry as one of the supporting materials for herbicides, pesticides, detergents and synthetic rubber. Based on these uses, the establishment of this monoisopropylamine factory is a good alternative to reduce import costs from abroad and support the development of domestic industry. The production method used in this Monoisopropylamine factory is the hydroamination method where the method reacts ammonia with dimethyl ketone and hydrogen in a fixed bed reactor. These reaction stages will produce Monoisopropylamine products and Diisopropylamine by-products. Next, the remaining hydrogen and ammonia will be separated using a flash drum and distillation I. Monoisopropylamine which is still mixed with Diisopropylamine will be separated in distillation II. High purity Monoisopropylamine is stored in the Monoisopropylamine storage tank while Diisopropylamine is separated again with water in Distillation III, so that the separated Diisopropylamine will be stored in the Diisopropylamine storage tank. The separated water will be used as cooling water feed for utilities.
| Item Type: | Thesis (Undergraduate) | ||||||||
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| Subjects: | T Technology > TP Chemical technology > TP155 Chemical engineering | ||||||||
| Divisions: | Faculty of Engineering > Departement of Chemical Engineering | ||||||||
| Depositing User: | Revita Revita Arendri | ||||||||
| Date Deposited: | 23 Jun 2025 03:43 | ||||||||
| Last Modified: | 23 Jun 2025 03:43 | ||||||||
| URI: | https://repository.upnjatim.ac.id/id/eprint/39019 |
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