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"A single phase, incompressible turbulent flow through a 90º pipe bend with/without guide vane conditions has been studied here. The present work deals with the numerical simulation to investigate the change in flow separation and velocity distribution at the downstream section due to the effect of the guide vane. The k-? turbulence model has been adopted for simulation purposes to obtain the results. After the validation of existing experimental and numerical results, a detailed study has been performed for three different Reynolds number and four different positions of the guide vane. The value of the Curvature ratio (Rc/D) has been considered as one factor for the present study. The curvature ratio can be defined as the ratio between the bend curvature radius and hydraulic diameter of the pipe. The results obtained from the present study have been presented in graphical form. A flow separation region has been found at the bend outlet for flow through 90º pipe bend without the guide vane. This flow separation region was absent for the cases which dealt with the flow through 90º pipe bend with the guide vane. Velocity distribution at four different downstream positions for different cases and different Reynolds numbers have been compared and reported in the present study."

"Peristiwa terjadinya letusan lumpur dan gas secara tidak terkendali dari lubang 150 meter dari LUSI (Lumpur Sidoarjo) sumur pengeboran eksplorasi hydrocarbon yang terus menerus keluar hingga ± 160.000 m³ per hari. Ketika laju aliran lumpur di dalam pipa berjalan lambat terjadi pengendapan pada bagian bawah, hanya cairan yang mengalir di atasnya. Sebaliknya, ketika aliran kecepatan terlalu tinggi menaikkan kerugian jatuh tekanan dan abrasi pada dinding pipa. Aliran dalam pipa spiral pada jarak langkah yang konstan menyebabkan aliran terus bercampur akibat perputaran sehingga dapat mencegah pengendapan. Tujuan dari penelitian ini yaitu untuk mengetahui kerugian jatuh tekanan (minor losses) dan distribusi kecepatan pada pipa circular lengkung dan spiral lengkung. Pengukuran distribusi kecepatan di dalam pipa spiral lengkung untuk dapat mengetahui proses pengendapan lumpur menggunakan alat pitot tube pada lokasi ? = 45º dan pengunaan manometer untuk mengukur minor loses. Minor losses yang terjadi pada pipa circular lengkung lebih kecil dibanding pada pipa spiral lengkung. Namun, untuk konsentrasi kepadatan lumpur 50%, pada Re = 2x10³ terjadi penurunan minor losses pada pipa spiral sehingga berhimpit dengan pipa circular. Distribusi kecepatan pada pipa circular lengkung berbeda dengan pipa spiral lengkung. Dimana untuk pipa circular lengkung, D = 24.6 mm terjadi ketebalan kecepatan minimum 0.42 m/s lebih besar dibanding ketebalan kecepatan minimum 0.36 m/s pada pipa spiral lengkung P/D = 6.7. Hal ini menunjukkan bahwa pada pipa circular lengkung pada kecepatan tertentu terjadi pengendapan sedangkan pada pipa spiral kengkung belum terjadi pengendapan. Variasi kepadatan Lumpur yang digunakan yaitu 50% dan 30%, dengan diameter rata-rata Lumpur adalah 5x10-³ mm.

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Events of mud and gas eruption is not controlled from the hole 150 metres from LUSI (Lumpur Sidoarjo) hydrocarbon exploration wells drilling continuing approximately 160,000 m³ per day. When the mud flow rate in the pipe slow subsidence occurred at the bottom, only the fluid that flows in pipe. Conversely, when the flow speed is too high increasing the pressure and the loss falls on the pipe wall abrasion. Spiral flow in a pipe at a constant distance measures the flow velocity due to continued mixing so as to prevent sedimentation.

The purpose of this study is to determine the loss of pressure fall (minor losses) and the velocity distribution in curved circular and curved spiral pipes. Measurement of velocity distribution inside the curved spiral pipe to know process of settling of the mud using a pitot tube at a ? = 45º and using manometer to measurement of minor losses. Minor loses that occur in curved circular pipe is less than the curved spiral pipe. However, for the concentration density of mud 50%, at Re = 2x10³ minor decrease spiraling losses in the pipe so that coincide with a round pipe.

Velocity distribution in curved circular pipe is different from the curved spiral pipe. Where to curved circular pipe, D = 24.6 mm occurred a minimum speed of 0.42 m/s greater than the thickness of a minimum speed of 0.36 m / s on the curved spiral pipe P / D = 6.7. This shows that the curved circular pipe at a certain speed while precipitation occurs in the curved spiral pipe has not occured. Mud density variations that are used are 50% and 30%, with an average diameter of Mud is 5x10-³ mm."

"Salah satu permasalahan utama yang terjadi dalam aliran fluida pada sistem perpipaan di industri adalah tingginya konsumsi daya pompa yang disebabkan oleh tingginya kerugian jatuh tekanan karena faktor gesekan dalam rezim aliran turbulen. Senyawa pengurang hambatan (DRA) digunakan sebagai salah satu solusi untuk mengurangi kehilangan daya dalam sistem perpipaan. Salah satu jenis DRA yang paling dikenal adalah biopolimer dengan keramahannya terhadap lingkungan dan ketersediaannya yang melimpah dan relatif murah.Penelitian ini bertujuan untuk mengetahui pengurangan kerugian jatuh tekanan dengan penambahan variasi konsentrasi larutan CMC dan suspensi fiber bacterial cellulose 250 ppm, 500 ppm, dan 750 ppm kedalam aliran minyak mentah pada pipa spiral dengan variasi rasio P/Di=3,5;5,4; dan 7,6, serta pipa bulat dengan Di = 17 mm. keefektifan DRA dapat dianalisis dengan pengukuran profil distribusi kecepatan.Hasil dari pengujian ini diperoleh nilai DR maksimum penambahan konsentrasi CMC pada konsentrasi 750 ppm untuk pipa bulat 35,8%, pipa spiral rasio P/Di 3,5=20,3%, P/Di 5,4=25,6%, P/Di 7,6=32,5%. Sedangkan penambahan bacterial cellulose pada pipa spiral rasio 7,6 diperoleh drag reduction maksimum sebesar 13 % dan pada pipa bulat sebesar 15 %. Peningkatan DR dapat ditunjukkan dengan data distribusi kecepatan aliran yang semakin tinggi dengan penambahan konsentrasi CMC yang semakin meningkat.

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One of the main problems that occur on the fluid flow in the pipeline industry is a high pump power consumption due to high frictional pressure drop in turbulent flow. Drag Reducing Agent (DRA) is used as one of the solutions to reduce the power losses in the piping system. One of the most popular DRA is biopolymer due to its environmentally friendly and inexpensive.This study aims to investigate the reduction of pressure drop using consentration of additive CMC and bacterial cellulose fiber suspension 250 ppm, 500 ppm and 750 ppm into crude oil flow in the spiral pipe with diameter ratio P/Di=3,5;5,4; and 7,6, and circular pipe with diameter Di=17 mm. The effectiveness of DRA could be analysed by measuring velocity distribution profile.The results of this test could be obtained maximum DR percentage of additives CMC of 750 ppm for circular pipe 35,8%, for spiral pipes with ratio P/Di 3,5=20,3%, P/Di 5,4=25,6%, P/Di 7,6=32,5% while, bacterial cellulose fiber suspension in spiral pipe with P/Di 7,6 obtained 13% maximum drag reduction and 15% in circular pipe . Increasing of DR could be presented by the data of velocity distribution profiles measurement that increased by increasing CMC concentration."