Main Article Content
Abstract
In the oil processing and manufacturing industry (PLTGU) in Indonesia, including PT.
PERTAMINA. Where the processing is in the form of crude oil, BBM (fuel oil). Non-Fuel,
Petrochemicals and oil and gas supplies, for the eastern part of Indonesia. One of the main
ingredients of this processing is water (H2O). Therefore, the location or location of industrial
plants must be close to raw water sources, namely sea water or the need for clean water
continuously andmaintained. Because the need forwateris very large, the flowof wateris made
according to the needs by building a pumping station. The water needed for cooling water is
then channeled to the main reservoir for raw materials for making oil. Pumps are used as a
tool to move fluids from one place to another through pipe media with changes in pressure on
the fluid. Pumps are usually for liquids. In the pump installation from the cooling tower
installation to the main reservoir is the Vogel centrifugal pump, where the head loss on the
suction pipe line is 0.8993 m, the head loss for the outlet pipe line is 1.211 m with a total head
loss of 0.825 m and the efficiency or performance of the pump G-31-41A centrifuge of 33.78%
Article Details
Copyright (c) 2024 puspawan angky; Muller Manurung Manurung, Agus Nuramal Nuramal
This work is licensed under a Creative Commons Attribution-ShareAlike 4.0 International License.
Authors who publish with this journal agree with the following terms:
- Authors retain copyright and grant the journal the right of first publication with the work simultaneously licensed under a Creative Commons Attribution License that allows others to share the work with an acknowledgement of the work's authorship and initial publication in this journal.
- Authors are able to enter into separate, additional contractual arrangements for the non-exclusive distribution of the journal's published version of the work (e.g., post it to an institutional repository or publish it in a book), with an acknowledgement of its initial publication in this journal.
- Authors are permitted and encouraged to post their work online (e.g., in institutional repositories or on their website) prior to and during the submission process, as it can lead to productive exchanges, as well as earlier and greater citation of published work (See The Effect of Open Access).
- This work is licensed under a Creative Commons Attribution-ShareAlike 4.0 International License.
References
-
[1]Anis, Samsudin dan Karnowo, 2008. Buku
Ajar Dasar Pompa, PKPUT UNNES,
Universitas Negeri Semarang.
[2] on, Bruce R., Young, Donald F., and
Okiishi, Theodore H., 1994. Fundamental of
Fluid Mechanic, Second Edition, John
Wiley & Sons, Inc. Canada.
[3] ite, Frank M., 2003. Fluid Mechanic,
Fitfh Edition, Mc Graw Hill, University
Rhode Island, USA.
[4] Sriyono, Dakso., 1996. Turbin, Pompa
dan Kompresor, PT. Erlangga, Jakarta.
[5] Sularso dan Haruo, Tahara, 2000.
Pompa dan Kompresor, PT.
PradnyaParamitha, Jakarta.
[6] Subramanya, K., 1993. Teory &
Applications of Fluid Mechanics, Fitfh
Edition, Tata-Mc Graw Hill Publishing
Company Limited, New Delhi
[7] Crittenden, John Charles, Trussell, R.
Rhodes, Hand, David W., Howe, Kerry J.,
Tchobanoglous, George, 2012. MWH’s
9
Treatment: Principles and Design, Third
Edition, John Wiley & Sons, Inc. Canada.
[8] Angky Puspawan, Agus Nuramal, Agus
Suandi, Nurul Iman Supriadi, 2016. Analysis
Of Headloss And Efficiency Of UGA-301 AB
Type Centrypugal Pump From Cooling
Tower Instalation To Dust Chamber On Urea
P-IV Maintenance Division (Case Study In
PT.PUPUK SRIWIDJAJA PALEMBANG CITY
SOUTH, Teknosia, UNIB.
[9] Angky Puspawan, 2015. Analisa RugiRugi Aliran Pada Instalasi Pipa Minyak Dari
Sumur Meruap 10(M.19) Ke Tangki
Dearator. Jurnal Telematik,7(4),1712-1756.
[10] Angky Puspawan, Syahlahudhin Al
Ayufhi, AgusSuandi, N.Iman supriadi,
Yovan Witanto, M. Chairun nawawi, 2018.
Analisa Headlosses Goulds 3196 Pompa
Sentripugal Dari Tangki Minyak Mentah Ke
Tangki Pengumpulan.Jurnal Rekayasa
Mekanik, 2(1).
[11] Angky Puspawan, Benny Dwika
Leonanda, 2022. Analisa Head Losses Dan
Efisiensi Pompa Sentrifugal Vogel Dari
Instalasi Menara Pendingin Ke
Penampang Utama.Juranl Inersia, 14(2).
References
Ajar Dasar Pompa, PKPUT UNNES,
Universitas Negeri Semarang.
[2] on, Bruce R., Young, Donald F., and
Okiishi, Theodore H., 1994. Fundamental of
Fluid Mechanic, Second Edition, John
Wiley & Sons, Inc. Canada.
[3] ite, Frank M., 2003. Fluid Mechanic,
Fitfh Edition, Mc Graw Hill, University
Rhode Island, USA.
[4] Sriyono, Dakso., 1996. Turbin, Pompa
dan Kompresor, PT. Erlangga, Jakarta.
[5] Sularso dan Haruo, Tahara, 2000.
Pompa dan Kompresor, PT.
PradnyaParamitha, Jakarta.
[6] Subramanya, K., 1993. Teory &
Applications of Fluid Mechanics, Fitfh
Edition, Tata-Mc Graw Hill Publishing
Company Limited, New Delhi
[7] Crittenden, John Charles, Trussell, R.
Rhodes, Hand, David W., Howe, Kerry J.,
Tchobanoglous, George, 2012. MWH’s
9
Treatment: Principles and Design, Third
Edition, John Wiley & Sons, Inc. Canada.
[8] Angky Puspawan, Agus Nuramal, Agus
Suandi, Nurul Iman Supriadi, 2016. Analysis
Of Headloss And Efficiency Of UGA-301 AB
Type Centrypugal Pump From Cooling
Tower Instalation To Dust Chamber On Urea
P-IV Maintenance Division (Case Study In
PT.PUPUK SRIWIDJAJA PALEMBANG CITY
SOUTH, Teknosia, UNIB.
[9] Angky Puspawan, 2015. Analisa RugiRugi Aliran Pada Instalasi Pipa Minyak Dari
Sumur Meruap 10(M.19) Ke Tangki
Dearator. Jurnal Telematik,7(4),1712-1756.
[10] Angky Puspawan, Syahlahudhin Al
Ayufhi, AgusSuandi, N.Iman supriadi,
Yovan Witanto, M. Chairun nawawi, 2018.
Analisa Headlosses Goulds 3196 Pompa
Sentripugal Dari Tangki Minyak Mentah Ke
Tangki Pengumpulan.Jurnal Rekayasa
Mekanik, 2(1).
[11] Angky Puspawan, Benny Dwika
Leonanda, 2022. Analisa Head Losses Dan
Efisiensi Pompa Sentrifugal Vogel Dari
Instalasi Menara Pendingin Ke
Penampang Utama.Juranl Inersia, 14(2).