INTEGRASI PANAS STEAM BREAKTHROUGH DAN BOILER DI SURFACE FACILITY PADA PERENCANAAN PROYEK INJEKSI UAP LAPANGAN BATANG

MARSETYO, MUHAMMAD MUFLIKH (2022) INTEGRASI PANAS STEAM BREAKTHROUGH DAN BOILER DI SURFACE FACILITY PADA PERENCANAAN PROYEK INJEKSI UAP LAPANGAN BATANG. Other thesis, UPN Veteran Yogyakarta.

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Abstract

Lapangan Batang telah diproduksikan selama 46 tahun namun recovery
factor (RF) hanya sekitar 14.73% pada 31 Mar 2020. Minyak yang dihasilkan
berupa minyak berat dengan 22,1o API. Selama ini produksi minyak dilakukan
menggunakan injeksi uap secara huff & puff dengan kualitas 70-80% pada
temperatur 400-500 oF dan tekanan ~300 psig. Produksi secara huff & puff kurang
optimum dan untuk meningkatkan RF diperlukan metode injeksi uap. Dalam
perencanaan injeksi uap diketahui akan terjadi steam breakthrough disumur
produksi. Steam breakthrough terproduksi perlu ditangani untuk diubah menjadi
kondensat air dan minyak terikut tidak mencemari lingkungan.
Permasalahan steam breakthrough dapat ditangani dengan memanfaatkan
panasnya untuk menaikkan panas fluida kerja air umpan Boiler. Sistem tersebut
terdiri dari pipa steam breakthrough dari sumur ke heat exchanger, Heat exchanger
sebagai media transfer panas kedua fluida, pipa fluida kerja dari heat exchanger ke
Boiler. Steam breakthrough berasal dari Sumur P3 dan P4 dengan total laju alir
volumetrik 3520 BCWEPD, laju alir massa 51304,25 lb/hr, tekanan dan temperatur
rata – rata 184,0 psig dan 44,25,8 oF. Laju alir volumetrik fluida kerja 3500
BCWEPD, laju alir massa 51012,7 lb/hr, tekanan 300 psig dan temperatur 89,6oF.
Jarak dari sumur breakthrough ke heat exchanger dengan panjang 3510 ft. Jarak
dari heat exchanger ke Boiler sepanjang 100 m.
Fasilitas pemanfaatan steam breakthrough terdiri dari pipa dari sumur ke
heat exchanger memiliki inside diameter 6,065 in dengan pressure drop 7,6 psi dan
hilang panas 5
oF. Heat exchanger tipe plate dengan luas transfer panas 900 ft2
dan
efisiensi 94,88%, pipa fluida kerja dari heat exchanger ke Boiler dengan inside
diameter 4,026 in dengan pressure drop 0,9 psi dan hilang panas 0,1 oF. Boiler
dengan temperatur fluida kerja masuk 89,6 oF memerlukan panas pembakaran
sebesar 1.476 MMBtu/hari dan biaya produksi Rp 214 juta/hari. Boiler dengan
tambahan heat exchanger memiliki temperatur fluida kerja masuk Boiler 349 oF
dan memerlukan panas pembakaran sebesar 1.035 MMBtu/hari serta biaya
produksi Rp 150 juta/hari. Pada analisa keekonomian didapatkan biaya investasi
heat exchanger sebesar Rp 4,70 milyar, biaya investasi Pipa sebesar Rp 5,09 milyar,
total biaya investasi sebesar Rp 36,3 milyar, keuntungan sebesar Rp 64.07 milyar
per hari maka didapatkan POT selama 1,5 tahun, NPV senilai Rp 20,90 milyar, IRR
sebesar 40% dan ROI sebesar 0,93.
Kata Kunci: Steam breakthrough, Heat exchanger, Boiler, pemanfaatan panas.

Item Type:	Thesis (Other)
Additional Information:	Steam breakthrough, Heat exchanger, Boiler, pemanfaatan panas
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Subjects:	T Technology > TA Engineering (General). Civil engineering (General)
Divisions:	Faculty of Engineering, Science and Mathematics > School of Engineering Sciences
Depositing User:	A.Md Sepfriend Ayu Kelana Giri
Date Deposited:	04 Oct 2022 06:33
Last Modified:	04 Oct 2022 06:33
URI:	http://eprints.upnyk.ac.id/id/eprint/31256

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