Capstone: the Tamarack Lake gathering system tie-in

Six months after joining the facilities group, Ethan presents his recommendation for the 04-22 tie-in to a review panel: Sofia, Mei Lin, Tom Ashworth, Wes Brandt for operations and the facilities manager. The question is simple to state. Should the new pad be tied in with a 6-inch or an 8-inch line, and what operating plan should go with it? Answering it brings together every part of the course: fluid properties, holdup, flow patterns, pressure drop methods, design codes and flow assurance.

This lesson works through the tie-in decision as a complete case study. It sets out the design basis, evaluates both candidate sizes over the production profile, checks each flow assurance threat, reviews the regulatory path and builds the operating plan. Along the way it shows how an engineer turns many partial results into a single defensible recommendation.

The design basis

The basis comes from the earlier lessons. The route is 6.2 km long with a net rise of 32 m to the battery, a low point at the creek crossing at 1.5 km and a 60 m climb to the ridge at 4 km (lesson 9). The fluids are a light Cardium oil of about 40 °API with associated gas and a water cut rising from 30 to 70 percent over ten years. Tom's forecast gives in-situ liquid rates falling from 1,100 to 260 m³/d and in-situ gas from 5,200 to 1,600 m³/d over the first ten years. The wellheads can deliver about 2,000 kPa initially, falling as reservoir pressure declines, and the battery inlet separator runs at 700 kPa. Ground temperature at burial depth falls to about 4 °C in late winter, and the hydrate formation temperature at line pressure is about 14 °C (lesson 10).

The pressure drop method is the one Ethan validated against the north pad line in lesson 7. For the screening calculations in this lesson he uses a simplified Beggs-Brill segregated holdup with a net-climb elevation term, which is fast enough to run for every year of the forecast; the detailed design will repeat the key cases with the validated mechanistic model and a transient simulator.

Hydraulics over the field life

# Capstone: compare 6-inch and 8-inch tie-in options for the new pad over the life of the field
import math
SI = True   
g = 9.81
L, climb = 6200.0, 32.0
rhoL, rhoG, muL = 880.0, 15.0, 0.003
years = [(1, 1100.0, 5200.0), (3, 700.0, 3600.0), (6, 420.0, 2400.0), (10, 260.0, 1600.0)]   # yr, in-situ liquid, gas m3/d
def dp(D, qLd, qGd, eps=4.6e-5):
    A = math.pi * D * D / 4
    vsl, vsg = qLd / 86400 / A, qGd / 86400 / A; vm = vsl + vsg; lam = vsl / vm
    NFr = vm * vm / (g * D)
    HL = min(0.98, max(lam, 0.98 * lam ** 0.4846 / NFr ** 0.0868))
    rho_ns = rhoL * lam + rhoG * (1 - lam); rho_s = rhoL * HL + rhoG * (1 - HL)
    Re = rho_ns * vm * D / (muL * lam + 1.2e-5 * (1 - lam))
    f = 0.25 / math.log10(eps / D / 3.7 + 5.74 / Re ** 0.9) ** 2
    return f * rho_ns * vm * vm / (2 * D) * L / 1000 + rho_s * g * climb / 1000, vm, HL
fp, up = (1, "kPa") if SI else (0.145038, "psi")
fv, uv = (1, "m/s") if SI else (3.2808, "ft/s")
for nps, D, cost in (("6-inch", 0.1541, 2.9), ("8-inch", 0.2027, 3.6)):
    print(f"{nps} option (installed cost about {cost} million {'Canadian' if SI else 'US'} dollars):")
    for yr, qL, qG in years:
        d, vm, HL = dp(D, qL, qG)
        inv = HL * math.pi * D * D / 4 * L
        print(f"  year {yr:2d}: dp {d * fp:5.0f} {up}, vm {vm * fv:4.1f} {uv}, holdup {HL:.2f}, liquid inventory " +
              (f"{inv:5.1f} m3" if SI else f"{inv * 6.2898:5.0f} bbl"))

6-inch option (installed cost about 2.9 million Canadian dollars):
  year  1: dp  1013 kPa, vm  3.9 m/s, holdup 0.34, liquid inventory  39.8 m3
  year  3: dp   521 kPa, vm  2.7 m/s, holdup 0.36, liquid inventory  41.1 m3
  year  6: dp   281 kPa, vm  1.8 m/s, holdup 0.37, liquid inventory  42.4 m3
  year 10: dp   187 kPa, vm  1.2 m/s, holdup 0.38, liquid inventory  44.2 m3
8-inch option (installed cost about 3.6 million Canadian dollars):
  year  1: dp   345 kPa, vm  2.3 m/s, holdup 0.39, liquid inventory  77.5 m3
  year  3: dp   222 kPa, vm  1.5 m/s, holdup 0.40, liquid inventory  80.1 m3
  year  6: dp   163 kPa, vm  1.0 m/s, holdup 0.41, liquid inventory  82.5 m3
  year 10: dp   142 kPa, vm  0.7 m/s, holdup 0.43, liquid inventory  86.0 m3

The results show the trade-off clearly. In year 1 the 6-inch line loses about 1,010 kPa, which the wells can supply: 700 kPa at the separator plus 1,010 kPa is about 1,710 kPa at the pad, within the 2,000 kPa available. The 8-inch line loses only about 345 kPa, which would let the wells flow against a lower back pressure and produce somewhat more early on. By year 10 the picture changes. The 6-inch line still flows at 1.2 m/s, holds about 44 m³ of liquid and loses 187 kPa. The 8-inch line has slowed to 0.7 m/s, below the 1 m/s guideline of lesson 9, holds about 86 m³ of liquid, and its pressure drop of 142 kPa is now almost entirely elevation loss on the climbs.

Two further hydraulic effects favour the smaller line late in life. First, the flow pattern: at the 6-inch line's year-10 velocity, the climbs remain in intermittent flow, which sweeps liquid over the ridge steadily, while the 8-inch line drops into stratified flow on the flats and slow, high-holdup flow on the climbs, the conditions that produce terrain slugging (lesson 11). Second, the inventory: every cubic metre of liquid held in the line must eventually be pushed out by a pig or a rate change, and the 8-inch line's larger inventory means larger pig slugs and longer, slower transients after shutdowns.

Back pressure and production

Tom raises the counter-argument. Lower back pressure in the early years means more production when the wells are most productive. Using the pad's inflow performance from his integrated model, he estimates that the 8-inch line would add about 2 to 3 percent to the first two years' oil, because the lower pad pressure lets the wells draw down further. Ethan compares this with the cost difference: the 8-inch line costs about 0.7 million Canadian dollars more installed. At current prices the extra early oil would roughly recover that cost over two years, so on early economics alone the two options are close.

The deciding factors are therefore the late-life operating costs and risks. Here the 6-inch line is clearly better: less liquid inventory, steadier flow on the climbs, smaller pig slugs, less water and sand settling at the creek crossing and so less corrosion risk, and a higher fluid temperature at the battery because the relaxation length depends on the mass rate per unit of pipe perimeter, which is higher in the smaller pipe. Several of these differences translate directly into costs: methanol, corrosion inhibitor, pigging labour, and the risk of a plug or a leak.

Flow assurance review

Mei leads the panel through the threats one at a time, using the approach of lessons 10 and 11.

Hydrates. In winter, both lines will operate below the hydrate formation temperature near the battery, and the creek crossing is the coldest point. The plan is to bury the crossing deeper than the standard depth, insulate the above-ground riser at the battery, and inject methanol at the pad in winter at a rate set by the Hammerschmidt check of lesson 10, adjusted with the field's own operating data. A written hydrate response procedure, including two-sided depressurization, will be in place before start-up. The 6-inch line's higher arrival temperature reduces the methanol rate.

Wax. At year-1 rates the fluid arrives well above the 22 °C (72 °F) wax appearance temperature. By about year 6, the downstream end of the line will drop below the WAT in winter. Pigging every two weeks, started from the first year to establish the deposition rate, will keep any deposit thin, and paraffin inhibitor will be evaluated if pigging returns show significant wax.

Slugging and pigging. The largest liquid arrivals will be pig slugs. For the 6-inch line, with an inventory of 40 to 44 m³ (250 to 280 bbl) at the screening holdup, a pig slug could be about half of that, far larger than the existing inlet separator can absorb. The plan therefore includes a dedicated slug catcher at the battery inlet, sized from a transient simulation of pigging at reduced rate, and a pigging procedure that slows the line during the pig's arrival. For the 8-inch line the slug catcher would need to be roughly twice as large.

Corrosion and sand. The produced water contains dissolved CO₂, and the uninhibited rates of lesson 11 would consume a 3 mm (120 mil) corrosion allowance in a few years. The plan specifies continuous corrosion inhibitor at the pad, corrosion coupons at the creek crossing and at the battery, and in-line inspection within the first five years. Temporary sand traps at the pad will handle proppant flowback from the new wells. Keeping the velocity above about 1 m/s (3 ft/s) on the climbs, as the 6-inch line does throughout the forecast, reduces both settling and under-deposit corrosion.

Regulatory path

The selected line will be licensed by the Alberta Energy Regulator (AER) under the Pipeline Act, with an application under Directive 056 that specifies the substance (multiphase oil effluent), maximum operating pressure, outside diameter, wall thickness, grade and route. Design, construction, pressure testing and operation will follow CSA Z662:23, and the line will be added to Prairie Crest's pipeline integrity management program, with the hazard assessment, inspection plan and inhibition program described above. Because the gas contains only trace hydrogen sulphide, the line does not require a separate emergency planning zone, but the licence application must still state the H₂S content. The AER's Directive 077 provides the reference tools for licensees, including requirements for pipeline records.

The recommendation

Ethan's recommendation is the 6-inch line, with the following operating plan: methanol injection at the pad in winter, deeper burial at the creek crossing and an insulated riser at the battery; continuous corrosion inhibitor and corrosion monitoring at the low point and the battery; pigging every two weeks from start-up, with a dedicated slug catcher sized from a transient pigging study; temporary sand handling at the pad during flowback; and a model validation plan that compares measured and predicted pressure drop quarterly, as he did for the north pad line.

He presents the risks honestly. If the production forecast proves high, the 6-inch line will be oversized late in life just as the 8-inch would have been, but less severely. If it proves low early on, the 6-inch line's higher back pressure costs less production than the panel feared. If the gas-oil ratio rises much more than forecast, the 6-inch line's friction could limit the pad in the early years; in that case a short loop line on the steepest section could be added later. Recording these sensitivities in the design basis lets future engineers see what was assumed and why.

Sofia's verdict is short. 'Smaller, steadier and cheaper to operate, with a plan for every threat we know about. Approved for detailed design.' Mei adds one condition: the transient pigging study must be complete before the slug catcher is ordered.

What the course has built

Looking back, each lesson contributed a piece of the decision. Lesson 1 framed the system from wellbore to battery. Lessons 2 and 3 provided single-phase friction and the definitions of holdup and slip. Lessons 4 and 5 described the flow patterns that set the physics in each part of the system. Lesson 6 split the pressure gradient into its components and showed which one dominates. Lessons 7 and 8 provided the empirical and mechanistic methods, and the discipline of validating them against field data. Lesson 9 applied them to sizing, velocity limits, code wall thickness and networks. Lessons 10 and 11 identified the threats that a line must survive, and this lesson combined all of it into a single recommendation with an operating plan.

The same workflow applies to other systems: a gas-condensate trunk line, a produced water disposal network, a horizontal well's tubing design or an offshore tie-back. The details change, but the steps are the same: define the basis, predict the flow patterns over the field life, choose and validate a pressure drop method, size for the whole profile, assess every flow assurance threat, satisfy the governing code and regulator, and write it all down so the operators who live with the line know why it was built that way.