pārekereke institute for research and development in māori and pacific education
Te Whare Wānanga o te Ūpoko o te Ika a Māui (The University at the head of the fish of Māui)
... Zealand School of Music Victoria has nine faculties, of which seven conduct teaching and research: Architecture and Design, Commerce, Education, Engineering, Humanities and Social Sciences, Law and ... are located at the Wellington Regional Hospital, in Newtown The Ferrier Research Institute and Robinson Research Institute are located at the Gracefield Science Campus, in Lower Hutt 10 University ... Certificate in Education and Professional Development 241 Postgraduate Diploma in Education and Professional Development 241 Master of Education (by thesis) 243 Master of Education...
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2012 Audit Plan: Finance, Audit and Facilities Committee Board of Regents doc
... focused industry training; Continue to lead and participate in the Pacific Northwest College and University Internal Audit Conference (hosted by UW for the past two years); and Continue to coordinate ... adequacy and effectiveness of the University’s system of internal control and the quality of the performance in carrying out assigned responsibilities including appropriate training and consulting ... implementing controls as described within their responses to Internal Audit report findings In selecting specific units/functions for inclusion in the audit plan we placed priority on providing coverage...
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surface production operations - design of oil handling systems and facilities
... the standard for the industry and have been used by thousands in every oil producing region of the world since their first printing We developed and taught two 5-day intensive continuing education ... with a gas eliminator on top before passing through the meter The meter contains devices for making temperature and gravity corrections, for driving the sampler, and for integrating the meter ... responsible for coordinating the entire typing and drafting effort Heri was also responsible for editing and pulling it all together at the end However, we take full responsibility for any errors...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
... SUP Initial FTP -Final FTP -Initial FIT -Final FTT -BHT Q8 Gas flow rate (Total 10 wells) Shut -in bottom-hole pressure Shut -in tubing pressure Initial flowing-tubing pressure Finalflowing-tubingpressure ... duty for oil treating, as well as to size heat exchangers for oil and water * Reviewed for the 1999 edition by K S Chiou of Paragon Engineering Services, Inc 8 Design of GAS-HANDLING Systems and ... systems A final thank you to Denise Christesen for her coordinating efforts and abilities in pulling this all together for us xii Preface As teachers of production facility design courses in petroleum...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
... be obtained directly from manufacturers A personal computer program for obtaining detailed physical properties of Therminol and for computing heat transfer coefficients and pressure drops in a ... temperature between the inside fluid bulk temper(text continued on page 20) 18 Design of GAS-HANDLING Systems and Facilities Table 2-2 Pipe Coil Data Norn, Size in 21A Sch No OD in !D in Internal Surface ... Equation 2-5 Tables 2-1 and 2-2 have basic tube and coil properties for use in Equation 2-5 and Table 2-3 lists the conductivity of different metals Inside Film Coefficient The inside film coefficient...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
... pitches for square patterns are % -in OD on 52 Design of GAS-HANDLING Systems and Facilities I -in and 1 -in OD on l!4 -in For triangular patterns these are % -in OD on % -in. , M -in OD on 1 -in. , and 1 -in ... inaccessible for inspection or mechanical cleaning The insides of the tubes can be cleaned in place by removing only the channel cover and using a rotary cleaner or wire brush Baffles Shell -and- tube ... diameter in inches within a very strict tolerance Heat-exchanger tubes are available in a variety of metals including steel, copper, brass, 70-30 copper-nickel, aluminum bronze, aluminum, and stainless...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf
... ft to 50 ft Tube Diameter — % in to H in Fins - ]A in to in height to 1 per in Depth — to rows of fin tubes Triangular pitch with fins separated by Me, in to !4 in Bay Widths — ft to 30 ft Fan ... Ft2 of Bundle Surface Area (APSF) for -in OD Tubes H in Height by fins /in % in Height by 10 fins /in Tube Pilch in A 2'/4 in A 21A in A 2'/£ in A rows rows rows rows 68.4 91.2 114.0 136.8 60.6 ... between the tubes and flame Heaters are not common in most field installations but are much more commonly used in plant situations in which competent operators routinely main tain and inspect the equipment...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps
... chemicals are polymeric 108 Design of GAS-HANDLING Systems and Facilities and include N-vinylpyrrolidone (5 ring), saccharides (6 ring}, and Nvinylcaprolactam (7 ring) An anti-agglomerator is an alkyl ... 0.00 0.87 0.5 05 1.22 Infinity 0.6 1.22 Infinity Figure 4-5 Approximate hydrate temperature formation (Courtesy of Smith Industries, Inc.) 100 Design of GAS-HANDLINCr Systems and facilities by Figure ... Reviewed for the 1999 edition by Kevin R Mara of Paragon Engineering Services, Inc 109 110 Design of GAS-HANDLING Systems and Facilities LTX UNITS These units are designed to allow hydrates to form and...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... liquids moving and to keep sand or other solids from settling and becoming a plugging problem The equation used for determining the pipe diameter is: where d = pipe inside diameter, in Z = gas ... The sizing of indirect fired heaters for these uses relies on the same principles and techniques discussed for wellstream line heaters 122 Design of GAS-HANDLING Systems and Facilities NOMINAL ... National Standard Institute (ANSI) B31.3 and B31.8, or American Petroleum Institute (API) Specification 12 K Volume has the tables for ANSI B31.3 and ANSI B31.8 Table 5-1 LTX Units and Line Heaters...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx
... tray, and gets increasingly richer in the heavy components and increasingly leaner in the light components The stabilized liquid is cooled in the heat exchanger by the feed stream before flowing ... set above random beds to prevent the pieces of packing from migrating or entraining upward Random packing comes in a variety of shapes and sizes For a given shape (design) of packing, small sizes ... 1 -in Raschig rings The 146 Design of GAS-HANDLING Systems and Facilities Figure 6-8 Various types of packing HETP for a 2 -in, slotted metal ring in a condensate stabilizer is about 36 in This is...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc
... it Monoethanolamine Systems Monoethanolarnine (MBA) is a primary amine that can meet nominal pipeline specifications for removing both H2S and CO2 MBA is a stable compound and in the absence of ... 7-3 The inlet gas line should have taps for gas sampling, temperature measurement, pressure measurement, and for an injection nozzle for Acid Gas Treating 181 Figure 7-12 Removal of H2S and C€>2 ... FOR AMINE SYSTEMS The types of equipment and the methods for designing the equipment are similar for both MEA and DBA systems For other amine systems such as SNPA-DEA, Fluor Econamine (DGA), and...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf
... dehydration used *Reviewed for the 1999 edition by Lindsey S Stinson of Paragon Engineering Services, Inc 195 196 Design of GAS-HANDLING Systems and Facilities for natural gas In producing operations gas ... U.S and to Ib/MMscf in Canada These values correspond to dew points of approximately 32°F for lb/ MMscf, 20°F for lb MMscf, and 0°F for Ib/MMscf in a 1,000 psi gas line Dehydration to dew points ... of GAS-HANDLING Systems and Facilities For design, reboiler temperatures in a stripper operating at 10 psig can be assumed to be 245°F for 20% MEA and 250°F for 35% DBA Amirie Stripper Amine strippers...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf
... bed being regenerated, one fresh bed adsorbing, and one bed in the middle of the drying cycle Internal or external insulation for the adsorbers may be used The main purpose of internal insulation ... requirements and costs Internal insulation eliminates the need to heat and cool the steel walls of the adsorber vessel Normally, a castable re factory lining is used for internal insulation The ... Piping, manifolds, switching valves and controls to direct and control the flow of gases according to the process requirements In the drying cycle, the wet inlet gas first passes through an inlet...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... machine in which the compressing and displacing element is a piston moving linearly within a cylinder Figure 10-1 shows the action of a reciprocating compressor In Position the piston is moving ... compressor ratio in the range of to 20 * Reviewed for the 1999 edition by John H Galey of Paragon Engineering Services, Inc, 253 254 Design of GAS-HANDLING Systems and Facilities In some marginal gas ... compressors, considerations for selecting a type of compressor, a procedure for estimating horsepower and number of stages, and some process considerations for both reciprocating and centrifugal compressors...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... Figure 10-11 Curve for estimating compression horsepower (Reprinted wirfi permission from GPSA Engineering Data Book, Wth Ed.) parts and personnel familiar with operating and maintenance, waste ... could influence the selection for a specific installation Procedure for More Accurate Determination of Horsepower and Number of Stages There are economic and operational reasons for considering ... additional cylinder or case, and more complex piping and controls In addition, there are some horsepower losses due to additional mechanical friction of the cylinder or rotating element and the increased...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... within the bearing that supports the load while allowing for rotation In a reciprocating compressor the bearing locations are: * Main bearings—between crankshaft and frame * Crank pin bearing—between ... the gas that remains in the cylinder in the fixed and added clearance areas expands until the pressure in the cylinder is equal to the pressure in the line outside of the cylinder The greater ... crankshaft and connecting rod * Wrist pin bearing—between connecting rod and crosshead * Crosshead bearing (shoe)—underneath the crosshead Packing Packing provides the dynamic seal between the cylinder...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf
... of GAS-HANDLING Systems and Facilities COOLING AND LUBRICATION SYSTEMS Compressor Cylinder Cooling Traditional compressor cylinder designs require cooling water jackets to promote uniform distribution ... bearings, connecting rod bearings, crosshead shoes, and can also supply oil to the packing and cylinder lubrication system Splash lubrication systems are 314 Design of GAS-HANDLING Systems and ... (2,500 ft/min) Volume contains the necessary formulas for determining pressure drop and velocity in gas piping Analog or digital simulators can be used to establish the pulsation performance of...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... platforms, and stairs - Vessel supports and lifting lugs - Insulation supports - Shop drawings • Fabrication - General - Welding - Painting - Inspection and testing - Identification stamping ... internals for their maintenance and/ or replacement Vessels 36 in and larger should have a minimum of one 18 -in manway Vessels 30 in and smaller should have two 4 -in flanged inspection openings Manway ... fireproofing or minimum inches The projection of sleeves shall be increased when necessary for reinforcing the skirt under certain loading conditions Diameter (0) = 16-24 inches PIPE OPENINGS The shape...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... relief fluids can be routed to a safe location for venting or flaring Piping should be installed in such a manner that liquid in the piping will drain into the header Relief valves should be located ... relieving If P2 increases because the valve is installed in a header system with other valves, then the amount of pressure in the vessel (the set point) required to overcome the spring force increases ... VALVE SIZING Most relief valve manufacturers have software available for sizing relief valves These programs are relatively easy to use Understanding how relief valves are sized and inputting the...
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