Shabazpur Gas Field at a Glance
Shahbazpur Gas Field was discovered by BAPEX (Bangladesh Petroleum Exploration and Production Company Ltd) in 1995 at Bhola, Bangladesh. The production was commenced in 11th May, 2009. In the earlier stage of production, the plant was based on LTX units till late 2014. In 2015, the plant was changed to TEG Dehydration unit base from LTX unit base due to the high condensate and water production rate. Till now, it has the highest production rate compared to the other gas fields owned by BAPEX.
Salient Features
Location : Borhanuddin, Bhola
Number of Wells: 04
Number of Producing Well: 03
Daily Production: 50 MMSCF (10 Jan, 2019)
Type of Process Plant: Glycol Dehydration
Capacity: 70 MMSCFD (2 x 35 MMSCFD Glycol Dehydration Tower)
Cumulative Production: 39.03 BCF (Dec, 2017)
Total Reserve: 1.6 TCF
Reservoir Condition
The Shahbazpur structure is a subsurface anticlinal structure situated in the middle of the Bhola Island in the northern margin of Hatia trough of Bengal Foredeep. The Hatia trough is bounded by the Chandpur-Barisal high in the northwest, and by the Chittagong-Tripura Fold Belt in the southeast. The alignment of the NW-SE trending oval shaped Shahbazpur structure is parallel to the Kutubdia structure which is located in Bay of Bengal to the south. Shahbazpur structure is surrounded by Muladi Structure to the Northwest and Kutubdia Structure to the Southeast. The structure started growing probably during Late Miocene and its acme of development took place during Mio-Pliocene sedimentation and ended in Pleisto-Pliocene time. This structure is relatively 69.4 m higher than the Kutubdia structure. The amplitude of the structure increases with depth. There is no surface expression of the Shahbazpur structure and the surface is floored with recent alluvial plain.
Reservoir Depth : 3480 m
Reservoir Pressure: 5400 psi
Reservoir Temperature: 195 F
Well Condition
There are four wells developed in Shahbazpur gas field. Three of them are currently under production while one well is under workover operation.
Tubing Diameter: 4.5 inches
Casing Diameter: 7 inches
Depth: 11480 ft
Figure 1: Wellhead of Well-3
Gas Composition
The sample was tested at 94 degF temperature and 540 psi pressure in BAPEX laboratory. The determined gas composition is taken as input for plotting phase diagram of the sample in ECLIPSE software. The generated phase diagram in figure-2 shows that cricondenbar (67 bar) is greater than critical pressure (58 bar). It clearly shows that the gas of SBZ gas filed is a dry gas reservoir.
Table-1: Gas Composition of SBZ Gas Field
Figure 2: Phase Diagram of Gas Sample
Process Flow Diagram and Process Units
A simple process flow diagram of SBZ gas field is illustrated below.
Figure 3: Process Flow Diagram of Shahbazpur Gas Field
Process Units
3-Phase Separator
Header
Water Bath Heater
2-Phase Separator
TEG Dehydration Tower
Sales Gas Scrubber
Condensate Flash Separator
Corrugated Plate Interceptor (CPI)
Pipe Schedules and Valve Rating
There are 5 types of scheduled pipes (XXS, 160, 120, 80 and 40) and 4 types of rated valves (#2500, #1500, #600 and #150) used in the SBZ gas field.
Daily Flow Calculation through Orifice Meter
The daily gas flow through the orifice is measured using the following formula. For better understanding, please read the article 6.7.10 (Flow Measurement) from the book 'Standard Handbook of Petroleum and Natural Gas Engineering' by William C. Lyons and Gary J. Plisga.
Rate of Flow, Qh = C`√(hwPf) in MMSCF/d where C` = Fb * Fpb *Ftb * Fg * Ftf * Fr * Y * Fpr * Fm
Fb = Basic Orifice Flow Factor
Fpb = Pressure Base Factor
Ftb = Temperature Base Factor
Fg = Specific Gravity Factor
Ftf = Flowing Temperature Factor
Fr = Reynold’s Number Factor
Y = Expansion Factor
Fpr = Supercompressibility Factor
Fm = Manomatric Factor
Input Variables:
Pipe Inner Dia (ID) in inch
Orifice Inner Dia (ID) in inch
Specific Gravity of Gas
Flowing Temperature (in F)
Gauge Pressure (in PSI)
Avg Differential Pressure (in H2O inch column)
Determining Optimum Gas Flow
For well no-2, the officials of SBZ gas field have manually found that considering all factors and variables the optimum flow rate is approximately 14 MMscf/d. But here, we have done an experimental simulation of optimum flow rate using ECIPLSE software and it came out 14.1 MMscf/d for THP of 400 psi which is close to the field result.
Input Variables:
Tube Dia = 4.5 in
Casing Dia = 7 in
WGR = 1.1229 bbl/ Mscf
CGR = 0.12 bbl/ Mscf
PI = 11.42 Mscf/ d. psi
SG of Water = 1.00
SG of Condensate = 0.9
SG of Gas = 0.5992
Max Flow Rate = 20 MMscf/d
Min Flow Rate = 5 MMscf/d
Reservoir Pr = 5400 psi
Figure 4: BHP vs Gas Flow with Linear IPR Curve for Well No. 2
Steps Followed in ECLIPSE Software to Determine the Optimum Flow
(Download Generated VFP Table)
Step-1: Input the Gas Composition
Step-2: Plot the Well Trajectory
Step-3: Input Temp Data against Tube Length
Step-4: Input PVT Data
Step-5: Input Required Data for BHP vs Flow Plot
Step-6: Choose Type of IPR Curve and Plot