PETE 310. Lectures # 33 & # 34 Chapter 17

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PETE 310 Lectures # 33 & # 34 Chapter 17

Gas Hydrates Prediction & Control

Hydrates Definition Natural gas hydrates are ice-like structures composed of water and natural gas molecules. Under favorable conditions of high pressure and low temperature, water molecules form cages which encapsulate gas molecules inside a hydrogen-bonded solid lattice

Why Study Gas Hydrates? Hydrates have potential as a future energy resource Energy stored in methane hydrates range from 350 to 3500 years supply

Why Study Gas Hydrates? Hydrates currently cause blocking in some underwater natural gas pipelines

Why Study Gas Hydrates? Affect strength of sediments in which they are found (care in constructing underwater structures) Subsidence Safety

Gas hydrates may cause landslides on the continental slope

Why Study Gas Hydrates? Hydrates have potential as a future energy resource

Why Study Gas Hydrates? Hydrates have potential as a future energy resource Related to climate change Affect strength of sediments in which they are found (care in constructing underwater structures) Hydrates currently cause blocking in some underwater natural gas pipelines Hydrates may be an alternative to pipeline transmission as a way to move natural gas from deep water to the terminals of existing offshore pipelines

World Wide Locations of Natural Methane Hydrate

Storage Capacity of Hydrates

A source of clean burning fuel?

Natural Gas Hydrate on the Sea Floor

Hydrates Occurrence in Petroleum Production Engineering Operations More common, est. $500 million just for inhibition in offshore pipelines Drilling Typically during well control situations external to BOP at seafloor Drill Stem Testing operations Typically in deeper water, but definitely possible in shallow water operations

Basics Of Gas Hydrates General Description Crystal Structure Thermodynamic inhibition Hydrate Phase Behavior And Inhibition Kinetic inhibition Prediction of the hydrate phase behavior Remedial Actions

Crystal Structure Cavities, guest, host

Crystal Structure of Gas Hydrates Gas Clathrates are crystalline compounds that occur when water forms a cage-like structure around smaller guest molecules.

Definitions Host - water molecules Guest - gas molecules

Methane Hydrate Molecular Structure

Hydrates vs Ice Different dielectric constant Different thermal conductivity HYDRATE: 2.23 W/m-K ICE: 0.5 W/m-K hydrate)

Hydrate Forming Conditions Hydrates can form when 4 ingredients are present: free water natural gas (N 2, H 2 S, CO 2, C 1, C 2, C 3, ic 4 ) reduced temperature increased pressure

Elements Necessary for Hydrate Formation Hydrate High Press. Water Low Temp. Natural Gas

Hydrate Modeling How much hydrate forms and when?

Hydrate Modeling Three-phase V-L-S equilibria Need models for fugacity coefficients (solid, liquid, gas) Hydrate formation curves f(p,t,composition) saturation boundary

Hydrate vs No-Hydrate Pressure Hydrate forms Hydrate does not form Temperature

Hydrate Equipment For measurement procedures see the following web site http://www.neosoft.com:6969/~westport/windowcell.html

Pressure /psi Typical Hydrate PT Curves 3000 Tranquitas Aguarague 2500 Valle Morado San Pedrito 2000 Madrejones Chango Norte 1500 Lomitas 1000 A B Porcelana Ramos Campo Duran 500 Ñacatimbay 0 30 40 50 60 70 T A Temperature /F T B Yacarecito La Bolsa

Typical Gas Compositions (mol %) Well C1 C2 C3 ic4 nc4 ic5 nc5 C6 + N2 CO2 Tranquitas 92.09 2.52 0.51 0.10 0.12 0.05 0.04 0.09 0.56 3.92 Aguarague 92.04 2.82 0.74 0.14 0.21 0.10 0.08 0.25 0.78 2.84 Valle Morado 88.29 3.05 0.65 0.24 0.30 0.14 0.14 0.28 3.93 2.98 San Pedrito 87.77 4.86 1.51 0.31 0.41 0.19 0.12 0.21 0.87 3.75

Pressure / psi Light Components Effect 1500 1300 1100 900 700 500 T = 50 F T = 60 F 300 80 85 90 95 100 Composition (N2 + CO2 + C1 ) / mol%

Hydrates: Remedies Once hydrates have formed what can be done to remove them? reduce pressure increase temperature chemical (thermodynamic) inhibition kinetic inhibitors mechanical removal

Hydrates: Prevention Remove any of the 4 ingredients Thermodynamic inhibitors electrolytes (salts) form ionic bonds with free water polar compounds (alcohols, glycols) compete with hydrates for hydrogen bonding

Thermodynamic Inhibitors Salts Alcohols Glycols

Hydrates: Prevention Salts Normally sodium chloride, 20-24% by wt. Potassium chloride can be used but it is significantly more expensive, and saturated KCl muds have performed poorly in offshore environments Calcium Chloride, very expensive and not as effective as NaCl for hydrate suppression

Salt Inhibitors Salt Ionizes In Solution And Interacts With The Dipoles Of The Water Molecules And Causes Clustering This Clustering Also Causes A Decrease In The Solubility Of Potential Hydrate Guest Molecules In The Water These Combine To Require Substantially More Subcooling To Cause Hydrates To Form Examples: Sodium Chloride And Calcium Chloride.

Alcohol Inhibitors The Hydroxyl Group Hydrogen Bonds The Water Molecules. In Direct Competition With The Dissolved Apolar Molecules Inhibition Ability - Decreases With Volatility Examples: Methanol Ethanol Isopropanol

Glycol Inhibitors More Hydrogen Bonding Opportunity With Water Through One More Hydroxyl Group Than Alcohols Glycols Generally Have Higher Molecular Weights Which Inhibit Volatility Examples Ethylene Glycol Triethylene Glycol

Common Thermodynamic Hydrate Inhibitors Salts NaCl KCl CaCl2 Na-Formate K-Formate NaBr CaBr2 ZnBr2 Alcohol/diols Methanol Ethanol Glycerol Ethylene glycol Propylene glycol Polyalkylene glycol

Thermodynamic Inhibitors Glycols Alcohols Salts Summary Alcohols & Glycols when dissolved in aqueous solutions form hydrogen bond with the water molecules and make it difficult for the water molecules to participate in the hydrate structure.

Pressure /psi Effect of NaCl 5400 4600 3800 3000 NaCl 12 wt% NaCl 10 wt% NaCl 5 wt% without NaCl T = 60 F 2200 1400 600 80 85 90 95 100 (N2 + CO2 + C1) composition/mol%

Pressure /psi Effect of Methanol 5000 4000 3000 Methanol 20 wt% Methanol 5 wt% Methanol 0 wt% 2000 1000 0 20 30 40 50 60 70 80 Temperature /F

Hydrate Inhibitors Salts - Effectiveness NaCl > KCl > CaCl 2 > NaBr > Na Formate > Ca Nitrate More Effective

Typical Sample Formulations Equilibrium F psi DT 20% NaCl + 10% Aqua-Col 45 5360 36.5 20% NaCl + 10% HF-100 44.9 5067 37.1 20% KCl 66.1 5580 16.7 10% KCl + 10% Aqua-Col 71.2 5245 11.1 10% KCl + 10% HF-100 70.2 5460 12.4 10% KCl + 10% NaCl 61.6 4936 20.2 10% KCl + 10% NaCl + 10% Aqua-Col 51.0 4825 30.6 10% Aqua-Col 79.2 5500 3.5 20% NaFormate + 10% Aqua-Col 50.6 4570 30.5 Seawater 80 5500 2.7

Kinetic Inhibitors Strategy An additive(s) that renders the formed into a pumpable slurry. hydrate Focused on emulsifying environmentally acceptable synthetic oils with the objective of having the synthetic oil coat the forming hydrates, preventing agglomeration.

Kinetic Inhibitors Delay the onset of formation Slow the rate of formation Prevent the agglomeration of hydrates (slush) Reduce the amount of hydrate that form Kinetic Inhibition Hydrate Hydrate

Hydrate References (with full articles) Kinetics of Gas Hydrate Formation and Decomposition http://woodshole.er.usgs.gov/project-pages/hydrates/ http://www.netl.doe.gov/technologies/oilgas/futuresupply/methanehydrates/2009gomjip/index.html

Pressure With inhibitor Without inhibitor Temperature

No Hydrates Forming 45 o line Hydrates Forming

Initial P =2200 psia Initial T = 150 o F Safe (no hydrate) final P = 350 psia and final T = 50 o F

Hydrates Summary Lots of research issues to pursue Be aware of hydrates Be prepared to prevent hydrate problems materials procedures contingencies site/job investigation

Remove one of the components needed for hydrates to form Hydrate High Press. Water Low Temp. Natural Gas

Phase Boundaries

Serious Effects of Gas Hydrates in Drilling Operations Plugging of choke and kill lines Formation of a plug at or below BOP, preventing monitoring of pressures below BOP Plugging tubing, downhole tools and wireline during DST operation Free water tied up with hydrates can cause thickening of the mud

PRESSURE (PSIA) Remedial Actions (Hydrate melting schemes ) Mechanical 1250 NO INHIBITOR WITH INHIBITOR Depressurization CHEMICAL INHIBITION Chemical Thermal 1000 750 HYDRATES STABLE THERMAL DE- PRESSURIZATION 500 HYDRATES 250 UNSTABLE 0 10 20 30 40 50 60 70 80 90 100 TEMPERATURE( F)

Inhibition of Hydrates

Pressure, Temperature Profiles Sea Water

Inhibition/ Dissociation of Hydrates Remove One Component i.e. Water, Gas IncreaseTemperature Decrease System Pressure Use an Inhibitor in the Water Phase (Thermodynamic)

Hydrate Forming Gases For a given T Hydrate formation P increases as HC size decreases