FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER

Direct Fired Heater Cude (DFCH) were operated on gathering stations in East Kalimantan provience has been studied. Two units DFCH A & B have the same design load capacity of 18.0 MMBTU / hr. DFCH serves to heat the liquid before it is processed further in other equipment for the separation of wa...

Full description

Saved in:
Bibliographic Details
Main Author: SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/16031
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:16031
spelling id-itb.:160312017-09-27T14:53:51ZFAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/16031 Direct Fired Heater Cude (DFCH) were operated on gathering stations in East Kalimantan provience has been studied. Two units DFCH A & B have the same design load capacity of 18.0 MMBTU / hr. DFCH serves to heat the liquid before it is processed further in other equipment for the separation of water and crude in the liquid. DFCH #A has been operating nearly 36 years since May 1975 and DFCH #B is the addition of new units in operation 15 years. Replacement of damage tube section should be performed every year on DFCH # A. DFCH # B is more reliable than # A, but caused of the CO level in the flue gas is higher than # A, then the efficiency DFCH #B is lower than #A. <br /> <br /> Computation was carried out using Lobo-Evans approach. The results of measurements and observations are analyzed referring to the standards of API 573 and journals. Numerical computation was developed by the author and the results were compared with FLUENTTM software. <br /> <br /> It is concluded that tubes deteroritation were resulted by exceed of tube metal temperature (TMT) due to insufficient heat transfer area on convective zone. This condition will speed up coke formation on the inside tube wall of the tube and excessive expansion of tube on the longitudinal direction that was restricted by heater wall. It is recommended to increase the pipe length in the convective zone and change the tube lay-out in the heater so the tube metal temperature (TMT) will not exceed the allowable design metal temperature (DMT) of 540oC to meet standard API STD 530 [15]. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Direct Fired Heater Cude (DFCH) were operated on gathering stations in East Kalimantan provience has been studied. Two units DFCH A & B have the same design load capacity of 18.0 MMBTU / hr. DFCH serves to heat the liquid before it is processed further in other equipment for the separation of water and crude in the liquid. DFCH #A has been operating nearly 36 years since May 1975 and DFCH #B is the addition of new units in operation 15 years. Replacement of damage tube section should be performed every year on DFCH # A. DFCH # B is more reliable than # A, but caused of the CO level in the flue gas is higher than # A, then the efficiency DFCH #B is lower than #A. <br /> <br /> Computation was carried out using Lobo-Evans approach. The results of measurements and observations are analyzed referring to the standards of API 573 and journals. Numerical computation was developed by the author and the results were compared with FLUENTTM software. <br /> <br /> It is concluded that tubes deteroritation were resulted by exceed of tube metal temperature (TMT) due to insufficient heat transfer area on convective zone. This condition will speed up coke formation on the inside tube wall of the tube and excessive expansion of tube on the longitudinal direction that was restricted by heater wall. It is recommended to increase the pipe length in the convective zone and change the tube lay-out in the heater so the tube metal temperature (TMT) will not exceed the allowable design metal temperature (DMT) of 540oC to meet standard API STD 530 [15].
format Theses
author SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN
spellingShingle SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN
FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
author_facet SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN
author_sort SUDIRMAN (NIM : 23107312); Pembimbing : Dr. Ir. H. Abdurrachim, IMAN
title FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
title_short FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
title_full FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
title_fullStr FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
title_full_unstemmed FAILURE ANALYSIS OF TUBE INSIDE CRUDE HEATER OF CABIN TYPE WITH HORIZONTAL TUBE AND NATURAL DRAFT BURNER
title_sort failure analysis of tube inside crude heater of cabin type with horizontal tube and natural draft burner
url https://digilib.itb.ac.id/gdl/view/16031
_version_ 1820737605535268864