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Title: | Analisis Kebutuhan Steam Pada Proses Pemanasan Air Umpan Ketel Uap Pada Unit Deaerator Di Ptpn Ii Pks Pagar Merbau |
Other Titles: | Steam Requirements Analysis for Boiler Feedwater Heating in the Deaerator Unit at PTPN II Pagar Merbau PKS |
Authors: | Chairi, Lufty Ariza April |
metadata.dc.contributor.advisor: | Nasution, Amirsyam Hermawan, Indra |
Keywords: | Boiler feed water;Dissolved oxygen;Deaerator;Air umpan ketel uap;Oksigen terlarut |
Issue Date: | Feb-2023 |
Publisher: | Universitas Medan Area |
Series/Report no.: | NPM;168130037 |
Abstract: | Steam adalah sejenis fluida yang merupakan fase gas dari air apabila mengalami pemasan sampai temperatur didih donawah tekanan tertentu. Air umpan boiler yang akan diubah menjadi steam di PKS PAGAR MERBAU berasal dari air sugai pengolahan air sungai menjadi air umpan boileer melewati beberapa tahapan yang sedimentasi, flokulasi, penyaringan, demineralisasi dan deaerasi proses-proses ini bertujuan untuk menghilangkan pengotor. Kadar garam, ion-ion dan gas-gas terlarut yang ada pada air laut.Salah satu parameter mutu air umpan boiler adalah kadar DO (Dissolved Oxygen) dengan standar pabrik maksimal 7,52 ppm, kadar DO (Dissolved Oxygen) yang tidak memenuhi standar dapat menyebabkan korosi pada boiler. Deaerator adalah sebuah alat yang bekerja untuk menghilangkan gas-gas terlarut yang bersifat korosif untuk mencegah korosi pada boiler. Deraerator bekerja berdasarkan sifat oksigen yang kelarutannya pada air akan berkurang dengan proses pemanasan yang mengakibatkan terjadinya kenaikan temperatur pada proses ini, bahan yang masuk berupa air dari feed water tank yang merupakan hasil pengolahan air (water treatment). Temperatur awal umpan yang masuk kedalam deaerator adalah 66ºC dengan konsentrasi oksigen terlarut sebesar 7,53 ppm berkontak langsung dengan steam yang berasal dari BPV dengan tekanan 1,7 Kg 𝑐𝑚 2 . Air umpan yang dihasilkan setelah dipanskan maka suhunya akan naik menjadi 82ºC dengan konsentrasi oksigen terlarut sebesar 7,25 ppm jumlah steam yang dibutuhkan pada proses pemansan air umpan boiler sebesar 766.675,7620 kkal/jam. Steam is a type of fluid which is the gaseous phase of water when it is heated to a boiling temperature and a certain pressure. Boiler feed water that will be converted into steam at PKS PAGAR MERBAU comes from river water processing river water into boiler feed water through several stages which are sedimentation, flocculation, filtering, demineralization and deaeration these processes aim to remove impurities. The levels of salt, ions and dissolved gases present in seawater. One of the parameters for the quality of boiler feed water is the DO (Dissolved Oxygen) level with a maximum factory standard of 7.52 ppm, the DO (Dissolved Oxygen) level does not meet the standard. can cause corrosion in the boiler. Deaerator is a tool that works to remove corrosive dissolved gases to prevent corrosion in the boiler. The deraerator works based on the nature of oxygen whose solubility in water will decrease with the heating process which results in an increase in temperature in this process, the incoming material is in the form of water from the feed water tank which is the result of water treatment. The initial temperature of the feed entering the deaerator is 66ºC with a dissolved oxygen concentration of 7.53 ppm in direct contact with steam coming from the BPV with a pressure of 1.7 Kg 𝑐𝑚 2. The feed water produced after being heated, the temperature will rise to 82ºC with a dissolved oxygen concentration of 7.25 ppm, the amount of steam needed in the boiler feed water heating process is 766,675.7620 kcal/hour. |
Description: | 69 Halaman |
URI: | https://repositori.uma.ac.id/handle/123456789/27825 |
Appears in Collections: | SP - Mechanical Engineering |
Files in This Item:
File | Description | Size | Format | |
---|---|---|---|---|
168130037 - Lufty Ariza April Chairi - Chapter IV.pdf Restricted Access | Chapter IV | 384.65 kB | Adobe PDF | View/Open Request a copy |
168130037 - Lufty Ariza April Chairi - Fulltext.pdf | Cover, Abstract, Chapter I, II, III, V, Bibliography | 1.95 MB | Adobe PDF | View/Open |
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