GPO Final Flashcards
In the flash vaporization process, condensate from the HP flash drum is sent to the:
1) MP flash tank
2) Rich solution flash tank
3) Incinerator as fuel
4) Condensate storage tank
1) MP flash tank
Stabilization by fractionation is a single tower process because:
1) The finished product from the bottom is composed mainly of butane.
2) Only one specification product is required.
3) Precise production of liquid of suitable vapour pressure is not necessary in the process.
4) Two specification products are required.
2) Only one specification product is required.
Condensate stabilizers are effective at:
1) Removing C1, C2 and C3 and H2S and CO2
2) Fractionization of C3 and C4
3) Fractionization of natural gasoline
4) All of the abov
1) Removing C1, C2 and C3 and H2S and CO2
Natural gasoline is in demand in the aviation field because:
1) Of the high propane content of the product
2) Of the lean absorption oil content of the product
3) Of the high vapour pressure of the product
4) Of the excellent octane characteristics of the product
4) Of the excellent octane characteristics of the product
Stabilization by fractionation makes a cut between the lightest liquid component and:
1) Pentane
2) Butane
3) Methane
4) Propane
2) Butane
Stabilization by fractionation is a single tower process since only one specification product is required.
1) True
2) False
1) True
In the flash vaporization process, vapour from the condensate stripper is sent to the:
1) Condensate storage tank
2) Rich solution flash tank
3) Incinerator
4) LP flash tank
3) Incinerator
Stabilization by fractionation makes a cut between the heaviest gas and:
1) Pentane
2) Ethane
3) Propane
4) Butane
1) Pentane
The removal of the methane, ethane, and propane from the stream and the reduction of butane content:
1) Increases the production of sales gas
2) Raises the condensate vapour pressure and lowers evaporation
losses
3) Decreases the production of sales gas
4) Lowers the condensate vapour pressure but increases evaporation losses
1) Increases the production of sales gas
Condensate stabilizers produce a product often referred to as:
1) Crude oil
2) Motor fuel
3) Natural gasoline
4) Natural gas liquids
3) Natural gasoline
In natural gasoline, the maximum allowable butane content, without a penalty, is usually:
1) 15% by volume
2) 0.5% by volume
3) 1.5% by volume
4) 1.75% by volum
3) 1.5% by volume
To ensure that the vapour pressure can be adjusted to the product customers desired level, gas plant finished gasoline contains small amounts of:
1) Methane
2) Octane
3) Propane
4) Butane
4) Butane
Equilibrium vaporization occurs when the vapour and liquid phases are in equilibrium at the:
1) Inlet of the fractionation tower
2) Initial temperature and pressure of separation
3) Highest point on the Reid Vapour Pressure scale
4) Final temperature and pressure of separation
4) Final temperature and pressure of separation
Condensate stabilization through the Flash Vaporization process is most likely to produce which product?
1) Butane and pentane
2) Butane and septane
3) Methane and ethane
4) Ethane and octane
3) Methane and ethane
What end-use or feed for flash gases is produced in the incinerator fuel stage:
1) H.P Condensate Flash Drum
2) M.P. Condensate Flash Drum
3) L.P. Condensate Flash Tank
4) Condensate Stripper
4) Condensate Stripper
The Natural Gas Processors Association has established 24 different grades of gasoline based on the:
1) Volatility and Composition of the product
2) Volatility and Reid Vapour Pressure of the product
3) Composition and Reid Vapour Pressure of the product
4) None of the above
2) Volatility and Reid Vapour Pressure of the product
Flash drums are employed in an inlet separation system to:
1) Eliminate the possibility of hydrate blockings.
2) Obtain the release of vapour contents from the hydrocarbon liquids.
3) Recover all liquids, regardless of the operating conditions in the separator itself.
4) Capture and recycle the vapour contents from the hydrocarbon liquids.
2) Obtain the release of vapour contents from the hydrocarbon liquids.
A liquid slug at the inlet separator has activated the high level alarm in the control centre. This is also likely to result in:
1) Liquid carry-over into the amine unit.
2) Activation of the raw gas inlet ESD valve.
3) Foaming in the separator.
4) Icing across the dump valve.
2) Activation of the raw gas inlet ESD valve.
The production from the well, brought into the plant at fairly high rate, is passed to the flare through the separator and later is diverted to the plant, warming up the lines. However, prolonged flaring may cause:
1) The flare lines to freeze with hydrates or plug off.
2) The drain valves to back up.
3) Slugging in the separator vessel.
4) A high level condition.
1) The flare lines to freeze with hydrates or plug off
On starting up a new plant, it will be necessary to pressurize the gathering lines and all equipment.
1) True 2) False
1) True
An effective method of controlling maximum liquid levels in separators is: 1) Shutdown of well(s).
2) Reduction of raw gas inlet rates.
3) Opening of the excess liquid control valve.
4) B and C.
5) A, B and C
4) B and C.
The purpose of a line separator downstream of a primary inlet separator is to:
1) Increase liquid capacity during slug conditions.
2) Increase recovery of flash vapours from hydrocarbon liquids.
3) Produce water carry-over with liquid hydrocarbons.
4) Increase liquid removal from inlet gas streams.
4) Increase liquid removal from inlet gas streams.
During a process upset, it may be necessary to flare some gas. What potential problem increases the longer the flare valve is open?
1) Hydrates
2) Slugging
3) Corrosion
4) Foaming
1) Hydrates
In an inlet separator, hydrates formed during prolonged flaring may be eliminated by:
1) Heating the gas stream.
2) Adding methanol to the gas stream.
3) Removing the water from the gas stream.
4) All of the above.
2) Adding methanol to the gas stream.
A condensate demethanizer is added to a gas plant inlet stream to:
1) Pass on condensate to the stabilizer feed drum.
2) Flash out any remaining light vapours.
3) Recycle the product back to the inlet separator feed drum.
4) All of the above.
4) All of the above.
Identify the process stream in C in the inlet separator below.
1) Raw Inlet Gas
2) Produced Water
3) Dry gas to HP Contactor
4) Liquid Hydrocarbon outlet
3) Dry gas to HP Contactor
It is highly recommended to know the shut down devices that are on an inlet gas facility.
1) True 2) False
1) True
Identify vessel D in the figure below.
1) Inlet Separator
2) Inlet Separator Hydrocarbon Flash Drum
3) Feed Gas Scrubber
4) Inlet Separator Water Flash Drum
4) Inlet Separator Water Flash Drum
When starting up inlet separation equipment, it may be necessary to open the inlet valve wide open to prevent the formation of hydrates in the wellhead, well tubing or processing equipment.
1) True 2) False
2) False
Heating of hydrocarbon liquids in a Dump Separator or Demethanizer will:
1) Eliminate formation of hydrates.
2) Flash light hydrocarbons.
3) Stabilize liquid hydrocarbons.
4) Recover additional liquid hydrocarbons.
2) Flash light hydrocarbons.
In major gas plants, the LPG and gasoline recovery section of the plant is designed to scrub the chilled gas stream with low molecular weight absorption oil and remove most of its liquefiable hydrocarbons and gasoline constituents. One prerequisite in LPG recovery is that both the gas stream and the circulating lean oil must be chilled before the _____________ process.
1) Absorption
2) Dehydration
3) Refrigeration
4) Amine
1) Absorption
Extracted acid gases removed from the gas stream in the sweetening section of a gas plant include all of the following except:
1) Liquefied petroleum gas (LPG).
2) Carbonyl sulphide (COS).
3) Mercaptans (RSH).
4) Hydrogen sulphide (H2S).
1) Liquefied petroleum gas (LPG).
In a gas plant that has no LPG and gasoline facilities, the gas dehydration method most likely to be used would be one that makes use of:
1) Refrigeration.
2) A trough of liquid desiccants.
3) Glycol solutions.
4) A bed of dry desiccants.
4) A bed of dry desiccants.
The modified Claus method is a sulphur recovery method in which one third of the hydrogen sulphide in the acid gas feed is burned completely to form:
1) Sulphur dioxide.
2) Carbon monoxide.
3) Sulphur monoxide.
4) Carbonyl sulphide.
1) Sulphur dioxide.
To remove water from gas using refrigeration, the gas stream is chilled by means of propane refrigeration to condense the water vapour and the heavier hydrocarbon vapours, such as propane, butane, and pentane. How is the water vapour kept from freezing after condensation?
1) The gas is sprayed with glycol at points ahead of the chillers.
2) The gas is infused with carbon disulphide (CS2).
3) The gas is directed through a bed of solid desiccants.
4) The pre-chilled gas is directed to the bottom of an absorption tower
1) The gas is sprayed with glycol at points ahead of the chillers
The first step in processing the feed gas after it enters the plant is the:
1) Removal of the sour and other undesirable gases from the feed gas stream.
2) Dehydration of the gas to reduce the water content.
3) Conversion of the H2S content to elemental sulphur.
4) Separation of its liquid components.
4) Separation of its liquid components.
Government regulations require sulphur recovery efficiencies of:
1) 100%
2) 95% to 97%
3) 88% to 90%
4) 98% to 99%
4) 98% to 99%
The ______________________ process removes undesirable gases such as hydrogen sulphide (H2S), carbon dioxide (CO2), small quantities of carbonyl sulphide (COS), and carbon disulphide (CS2).
1) Dehydration
2) Gas sweetening
3) Refrigeration
4) Glycol
2) Gas sweetening
Which of the following auxiliaries may be required for a gas processing facility?
1) Garbage disposal, water disposal, bear control
2) Steam generating facilities, electrical generation facilities, water supply
3) Fire station, mail services, refueling station
4) Water heating, electrical generation, garbage disposal
2) Steam generating facilities, electrical generation facilities, water supply
In modern gas plants, what process does the industry generally favour as the best single step for preparing the gas stream for LPG recovery and removal of a large portion of gasoline constituents?
1) Glycol
2) Solid desiccants
3) Condensate stabilization
4) Refrigeration
4) Refrigeration
Of the three auxiliary processes discussed in this module, it is the _________ generation process that is essential to sour gas processing and treatment.
1) Water
2) Steam
3) Electrical
2) Steam
In a deep-cut facility, the LPG recovery process makes use of a:
1) Catalytic reactor and a bauxite catalyst bed.
2) Turboexpander and condensate stabilization.
3) Turboexpander and cryogenic principles.
4) Condensate stabilization facility and cryogenic principles.
3) Turboexpander and cryogenic principles.
Steam generation is absolutely necessary for sour gas processing and treatment.
1) True 2) False
1) True
One pre-requisite in LPG recovery is that:
1) The gas stream and the circulating lean oil must be chilled before the absorption process.
2) Only the gas stream must be chilled before the absorption process.
3) The gas stream and the circulating lean oil must be chilled after the absorption process.
4) Only the lean oil stream must be chilled after the absorption process.
1) The gas stream and the circulating lean oil must be chilled before the absorption process.
The feedstock of acid gases matches with which gas processing plant component?
1) Gas Sweetening
2) Sulphur Plant
3) Condensate Stabilization
4) NGL Fractionation
2) Sulphur Plant
The lean oil from the fractionator bottoms supplies heat to the deethanizer side reboilers before being cooled.
It is then:
1) Presaturated with deethanizer residue gas.
2) Mixed with the rich absorption oil in the absorber base.
3) Circulated as lean absorption oil at a fairly low temperature.
4) Injected ahead of the heat exchangers and chillers to prevent hydrate formation
1) Presaturated with deethanizer residue gas.
The feedstock of low temperature natural gas liquids matches with which gas processing plant component?
1) Gas Sweetening
2) Sulphur Plant
3) Condensate Stabilization
4) NGL Fractionation
4) NGL Fractionation
In the chillers, the heavier hydrocarbons are condensed at:
1) 29°C.
2) -39°C.
3) -29°C.
4) -9°C
3) -29°C.
Fractionation is the term used in the:
1) Separation of liquid hydrocarbons from produced water.
2) Removal of mercaptans and water from LPGs.
3) Recovery of NGLs from a natural gas stream.
4) Separation of NGLs into specific hydrocarbon components.
4) Separation of NGLs into specific hydrocarbon components.
The feedstock raw inlet condensate matches with which gas processing plant component?
1) Gas Sweetening
2) Sulphur Plant
3) Condensate Stabilization
4) NGL Fractionation
3) Condensate Stabilization
During fractionation, the resultant propane and butane products are individually treated to:
1) Presaturate the absorption oil before chilling.
2) Remove mercaptans and water before storing.
3) Recover the raw hydrocarbon product from the absorption oil.
4) Prevent hydrate formation and to dry the gas
2) Remove mercaptans and water before storing.
Identify the piece of equipment associated with the LPG recovery process:
1) Catalytic converter
2) LP amine contactor
3) Lean oil absorber
4) Depropanizer
3) Lean oil absorber
In the HP contactor of the gas sweetening stage, the sour gas is contacted with a sweetening agent by:
1) Circulating counter-currently in the towers.
2) Flashing off the methane content in the condensate demethanizer.
3) Refrigerating and mixing with the rich absorption oil in the absorber base.
4) A series of distillations, designed to separate the sour gas from the stream.
1) Circulating counter-currently in the towers.
To separate propane from recovered natural gas liquids tight control of designed _______________ and _______________ must be maintained in the depropanizer.
1) Pressure, flow rate
2) Flow rate, liquid levels
3) Temperature, pressure
4) Liquid levels, temperature
3) Temperature, pressure
In the stabilizer, the light ends are removed from the top and the bottom stabilized condensate product flows to storage to be regenerated in a still for further treating duties.
1) True 2) False
2) False
The lean glycol from the glycol regenerator is returned to the chillers while the water vapour is:
1) Re-circulated to the HP contractor.
2) Vented to the atmosphere.
3) Fed back to the chillers to aid in cooling.
4) Flashed to the reabsorber
2) Vented to the atmosphere.
Identify the piece of equipment associated with the fractionation process:
1) Catalytic converter
2) LP amine contactor
3) Lean oil absorber
4) Depropanizer
4) Depropanizer
The viscosity of sulphur is at its highest viscosity at 154°C. 1) True 2) False
2) False
In Alberta, license requirements governing sulphur recovery from sour gases are established by the:
1) APEGA.
2) WCB.
3) ERCB.
4) Ministry of Mines, Minerals and Resources.
3) ERCB.
The world demand for sulphur is dependent on:
1) Agricultural demand for fertilizers.
2) Sustained economic activity.
3) Demand for petroleum gases.
4) Regulated rates of sulphur from H2S.
2) Sustained economic activity.
The principle sulphate is:
1) Limestone.
2) Pyrite.
3) Gypsum.
4) Calcite
3) Gypsum.
The melting point of sulphur is exactly 119°C.
1) True 2) False
2) False
The industry that consumes the most sulphur production is:
1) Pulp and paper.
2) Chemical manufacturing.
3) Fertilizer.
4) Petroleum.
3) Fertilizer.
During the early afternoon, a heat sensor alarm has gone off in a sulphur block storage facility. There is obviously a fire somewhere in the sulphur blocks being stored outside. The sensor covers a large number of sulphur blocks. What would be the quickest way to find the fire?
1) Touch the sulphur blocks until you find the hot one.
2) Find the source of the acrid odour.
3) Look for a bright yellow flame.
4) Look for a blue flame.
2) Find the source of the acrid odour.
Elemental sulphur produced from sour gas may be hazardous due to:
1) It being a friable solid which breaks easily.
2) Its characteristic of being extremely hot in liquid form.
3) Its ability to absorb H2S and SO2.
4) The fact that it burns with a soft blue flame invisible in daylight.
4) The fact that it burns with a soft blue flame invisible in daylight.
Sulphur is not attacked by hydrochloric acid, except in the presence of large amounts of:
1) Air.
2) Lead.
3) Zinc.
4) Iron.
4) Iron.
At approximately 154°C the liquid sulphur becomes dark brown in colour, and its:
1) Viscosity is at its minimum.
2) Odour is undetectable by smell.
3) Vaporization rate is drastically reduced.
4) Viscosity is at its maximum.
1) Viscosity is at its minimum.
At which temperature does sulphur reach its highest viscosity?
1) 154°C
2) 293°C
3) 193°C
4) 119°C
3) 193°C
Refer to the graph below. Between the temperature of 120 to 160°C the viscosity of liquid sulphur:
1) Increases.
2) Remains the same.
3) Is at its maximum.
4) Decrease.
4) Decrease.
At normal atmospheric temperature, sulphur appears as a:
1) Yellow and crystalline liquid.
2) Yellow and crystalline solid.
3) Straw-yellow transparent liquid.
4) Dark brown and crystalline solid.
2) Yellow and crystalline solid.
Concentrated sulphuric acid in contact with sulphur will liberate sulphur dioxide at:
1) 200°C.
2) 250°C.
3) 100°C.
4) 1200°C.
1) 200°C
Today the primary reason for conversion of H2S into elemental sulphur is:
1) Economic benefit
2) Manufacturing industry demand for product
3) Government regulations
4) Safe handling of H2S
3) Government regulations
In a refluxed stabilizer when the vapour pressure of the natural gasoline gets too high:
1) The setpoint of the stabilizer bottom temperature controller is raised to increase the fuel to the heater.
2) The setpoint of the stabilizer feed drum pressure controller is raised to increase the pressure in the drum.
3) The setpoint of the stabilizer reflux accumulator level controller is raised to increase the reflux rate to the tower.
4) The setpoint of the stabilizer bottom temperature controller is lowered to decrease the fuel to the heater.
1) The setpoint of the stabilizer bottom temperature controller is raised to increase the fuel to the heater
In order to avoid flame impingement on the tubes of a fired heater:
1) The fuel gas pressure must be increased.
2) An adjustment to the air dampers below the burners is occasionally required.
3) The excess air supplied to the heater must be removed.
4) The air dampers below the burners must be fully closed.
2) An adjustment to the air dampers below the burners is occasionally required.
In a refluxed type of stabilizer, when the vapour pressure of the gasoline becomes too high, it means that the:
1) Set point of the stabilizer bottom temperature controller must be lowered.
2) Butane content is too low.
3) Set point of the stabilizer overhead temperature controller must be lowered.
4) Butane content is too high.
4) Butane content is too high.
The bottom temperature in a condensate stabilizer is kept close to:
1) 400°C.
2) 150°C.
3) 300°C.
4) 200°C.
4) 200°C.
Specific gravity is measured by an instrument called a:
1) Micrometer.
2) Dynamometer.
3) Manometer.
4) Hydrometer.
4) Hydrometer.
To detect the presence of free sulphur in gasoline, plant laboratory personnel conduct a:
1) Reid vapour pressure test.
2) Dryness test.
3) Copper strip test.
4) Specific gravity tes
3) Copper strip test.
The reflux rate to the tower is controlled by a flow controller set by the:
1) Inlet flow at the surge tank.
2) Liquid level of the reflux accumulator.
3) Overhead condensate levels at the damper.
4) Liquid level at the LP contactor.
2) Liquid level of the reflux accumulator.
Flame impingement on the tubes may be indicated by:
1) High temperature alarms.
2) Excess condensate outlet temperature.
3) Visible smoke from the heater’s stack.
4) Visible hot spots on the tubes.
4) Visible hot spots on the tubes.
To remove mercaptans from condensate in a stabilization tower, the reflux rate needs to:
1) Be shut off completely.
2) Be increased.
3) Be decreased.
4) Remain constant
2) Be increased.
The condensate to storage temperature in a condensate stabilizer system is maintained in the:
1) 93-121°C range.
2) 66-77°C range.
3) 27-38°C range.
4) 204-232°C range.
3) 27-38°C range.
Regardless of which start-up method is used to start the stabilizer process, the feed tank should be ready to: 1) Receive the flashed vapour and dispose of the condensate.
2) Allow liquid to collect in the top of the stabilizer.
3) Receive condensate and dispose of the flashed vapour.
4) Allow the feed to flow at maximum rate.
3) Receive condensate and dispose of the flashed vapour.
Excessive concentrations of heat at the tube fins in a fired heater may cause:
1) Liquid surging.
2) Internal coking and weak spots.
3) Hydrate formation.
4) External coking and weak spots.
2) Internal coking and weak spots.
The purpose of grounding condensate transport trucks is it:
1) Enables loading pumps to run.
2) Provides truckers indication of tank level.
3) Informs Control Centre of loading operations.
4) Eliminates static electricity
4) Eliminates static electricity
When loading or unloading condensate, any spills must be cleaned up after the truck driver has started his engine and driven off plant property.
1) True 2) False
2) False
The liquid feed to the stabilizer feed drum is usually maintained above 15°C in order to avoid:
1) Contamination of the reflux.
2) Hydrate plugging in the vapour outlet line when the pressure is dropped.
3) Contact between the water and condensate.
4) Hydrate plugging in the vapour outlet line when the pressure is increased.
) Hydrate plugging in the vapour outlet line when the pressure is dropped.
The truck driver is not required to be in attendance during the loading or unloading of condensate.
1) True 2) False
2) False
A gas booster plant is a compression plant that uses a number of compressors to:
1) Decrease the gas pressure for transmission purposes.
2) Strip off the valuable liquefiable products of ethane, propane, butane and gasoline.
3) Pump residue gas at high pressure into the reservoir, promoting recovery of liquid hydrocarbons.
4) Increase the gas pressure for transmission purposes.
4) Increase the gas pressure for transmission purposes.
Gas processing plants must be able to:
1) Withstand high operational pressures.
2) Be completely automated.
3) Remove small amounts of acid gases from the feedstock.
4) Run with completely sealed equipment units that are only accessible to highly trained contract maintenance personnel from outside the company.
1) Withstand high operational pressures.
Identify part A from the three major pieces of equipment contained in a gas cycling plant.
1) Oil Absorber
2) Compression Plant
3) Separation Plant
2) Compression Plant
In the illustration of a Gas Cycling Plant that has been designed with a Gas Sales System (shown below), the residue gas from the absorber is fed through the ___________ and ________________ into the injection well.
1) HP gas coolers, Heater
2) Heater, sales gas separator
3) HP scrubber, compressors
4) Reabsorber, absorber
3) HP scrubber, compressors
Gas processing plants must be able to complete the following functions to ensure that the sales contracts will be met.
1. Acid gas removal 2. Operate at high pressures 3. Handle large volumes of gas 4. Liquefy sulphur 5. Equipment is designed for inspection and maintenance 6. Flare any excess gas that cannot be sent to sales
1) 3, 4, 5, 6
2) 1, 2, 5, 6
3) 1, 2, 3, 5
4) 2, 3, 4, 5
3) 1, 2, 3, 5
Identify part C from the three major pieces of equipment contained in a gas cycling plant.
1) Oil Absorber
2) Compression Plant
3) Separation Plan
1) Oil Absorber
Rich and lean oil streams in gas plants are differentiated by their level of sulphur.
1) True 2) False
2) False
Of the following, which is not an important function of a natural gas plant?
1) To receive the sour natural gas from underground geological reservoirs and remove all objectionable impurities
2) To reduce the water content of raw gas to the level that ensures maximum separation process efficiency
3) To separate and remove certain constituents such as ethane, propane, butane and condensate
4) To repressurize the gas to a specified pressure for transmission purposes
2) To reduce the water content of raw gas to the level that ensures maximum separation process efficiency
The purpose of dehydrating a gas is:
1) To prepare the gas for re-injection back into the formation.
2) To remove the hydrocarbon condensate.
3) To remove H2S.
4) To remove the water.
4) To remove the water.
In the illustration shown below, after the water is separated from the gas flow, the raw gas from the wells enters the gas sweetening process, where the sulphur is ________ and sent to market.
1) Recovered
2) Dehydrated
3) Sweetened
4) Refrigerate
1) Recovered
A plant that is designed to pump residue gas at high pressure into the reservoir to promote the recovery of additional liquid hydrocarbons and to maintain the reservoir pressure at a desired level is known as a gas:
1) Repressuring plant.
2) Booster plant.
3) Stripping plant.
4) Straddle plant
1) Repressuring plant.
Aside from its other processes, a conventional gas processing plant may be equipped with facilities to:
1) Process rich crude oil streams.
2) Convert the hydrogen sulphide to elemental sulphur.
3) Convert the elemental sulphur to hydrogen sulphide.
4) Inject wet gas back into the formation.
2) Convert the hydrogen sulphide to elemental sulphur.
Control of the dewpoint in the sales gas is attained by a: 1) Straddle plant.
2) Deep cut plant.
3) Stripping plant.
4) Dehydration plant
4) Dehydration plant
Since gas plant processes result in drastic gas pressure reduction, gas plants must be capable of _________________ the gas for transmission purposes.
1) Depressurizing
2) Re-pressurizing
3) Removing the gasoline
4) Re-injecting
2) Re-pressurizing
The type of gas plant that receives a rich gas stream, usually from a pipeline carrier, and after removing the liquid hydrocarbons, re-injects the lean gas back to the pipeline is known as a:
1) Gas stripping plant.
2) Gas cycling plant.
3) Gas booster plant.
4) Gas injection plant
1) Gas stripping plant.
The most popular dehydration processes today are solid desiccants, glycol scrubbing, and:
1) Re-injection.
2) Recycling.
3) Refrigeration.
4) Boosting
3) Refrigeration.
In a Claus process straight-through plant that is equipped with condensers and converters using hot gas mixing valves and final stage steam reheat, the acid gas containing hydrogen sulphide enters the sulphur unit through the acid gas knockout drum. The flow then moves to the:
1) No. 1 condenser.
2) 3-way mixing valve.
3) Reaction furnace burner.
4) No. 2 condenser.
3) Reaction furnace burner.
In a split-flow Claus process plant, all of the H2S feed to the furnace is oxidized to sulphur dioxide. The effluent from the furnace equals about:
1) 10% of the 1/3 volume.
2) 20% of the 1/3 volume.
3) 10% of the 2/3 volume.
4) 20% of the 2/3 volume
2) 20% of the 1/3 volume.
In a straight flow-through sulphur recovery unit, combustion in the reaction furnace differs from a split flow process in that the combustion:
1) Occurs in a sub-stoichiometric condition.
2) Occurs at higher temperatures.
3) Occurs at a higher efficiency.
4) Occurs at a lower efficiency.
2) Occurs at higher temperatures.
The purpose of the incinerator is to burn any remaining SO2 to H2S. 1) True 2) False
2) False
The split-flow process works by dividing the acid gas stream into two portions. One portion, which is 1/3 of the total volume, is fed directly into the reaction furnace burner. The remaining 2/3 is fed into the:
1) Tail gas incinerator.
2) First condenser.
3) Waste heat boiler.
4) First converter.
4) First converter.
Liquid sulphur is kept molten in underground sulphur pits. To keep this sulphur in a liquid state, the use of steam coils is used to keep the sulphur liquid.
1) True 2) False
1) True
In a Claus process straight-through plant, when the gas stream leaves the No. 2 condenser, it is mixed with hot gas that is at a temperature of:
1) 896°C.
2) 138°C.
3) 220°C.
4) 480°C.
4) 480°C.
H2S is converted to SO2 in the incinerator furnace by: 1) Catalytic reaction.
2) Combustion at high temperatures.
3) Reaction with remaining SO2.
4) Reaction with fuel gas.
2) Combustion at high temperatures.
The primary purpose of condensers in a sulphur recovery process is:
1) To cool the effluent gas prior to entering the converter beds, thus improving conversion efficiency.
2) Recovery of heat generated in the exothermic reactions occurring in the SRU.
3) Removal of S2 from effluent vapours.
4) To generate steam for use in the processing plant.
3) Removal of S2 from effluent vapours
The acid gas feed to the plant’s Sulphur Recovery Unit is made up of 28% CO2 and 72% H2S. The type of sulphur recovery process used would be: 1) Split Flow.
2) Straight Flow.
3) Direct Oxidation.
4) Hot Gas By-Pass.
2) Straight Flow.
The sulphur recycle and the direct oxidation processes are similar to other Claus processes. However, in these two processes, to avoid hydrocarbon contamination of the converter beds, in the sulphur recycle plant:
1) No fuel gas is used to provide combustion.
2) SO2 is added to the stream.
3) CO2 is added to aid in combustion.
4) Sulphur is burned to provide SO2.
4) Sulphur is burned to provide SO2.
All of the following are advantages of a straight through process except one statement. Select the statement that is incorrect.
1) The process is ideally suited to acid gas flows in excess of 50% H2S.
2) Capable of 98 − 99% sulphur recovery.
3) The first converter operates at a much higher temperature improving sulphur recoveries.
4) The process has been simplified with fewer instruments and controls
3) The first converter operates at a much higher temperature improving sulphur recoveries.
In a split flow Sulphur Plant with acid gas having an H2S content of 15%, both air and acid gas are preheated to: 1) Vapourize water.
2) Directly oxidize H2S to SO2.
3) Increase efficiency of sulphur recovery.
4) Stabilize combustion in reaction furnace.
4) Stabilize combustion in reaction furnace
In a very lean feed plant, the effluent gases from the boiler are cooled to: 1) 220°C.
2) 205°C.
3) 370°C.
4) 250°C.
4) 250°C.
Seals on sulphur outlet lines from condensers are used to:
1) Maintain desired temperature in the condenser.
2) Prevent steam mixing with effluent vapours.
3) Prevent effluent gases from being emitted to the atmosphere.
4) Prevent S2 from solidifying.
3) Prevent effluent gases from being emitted to the atmosphere.
The highest level of S2 recovery from the acid gas is observed by:
1) Tight control of the air to acid gas ratio.
2) The lowest fuel requirements in the incinerator stack
3) The highest amount of sulphur produced.
4) The lowest SO2 emission rate from the incinerator stack.
4) The lowest SO2 emission rate from the incinerator stack.
Most plants use the air to acid gas ratio as the primary control for load changes. To trim the air to acid gas ratio when running in a steady condition, sulphur plants can make use of tail gas:
1) Analyzers.
2) Clean-up units.
3) Boosters.
4) Pumps.
1) Analyzers.
The Continuous Stack Emission Monitor records:
1) H2S to SO2 ratio.
2) Air demand.
3) Total SO2 released to the atmosphere.
4) Total SO2 and H2S released to the atmosphere.
3) Total SO2 released to the atmosphere
In Alberta, Alberta Environment requires all sulphur plants to have ambient air quality monitoring done at a specified location:
1) Downwind of the plant.
2) Inside of the plant.
3) Upwind of the plant.
4) In a sheltered location beside the plant.
1) Downwind of the plant.
After the stream has passed through the converter, heat generated from the reactors is transferred to feed water or steam in the condenser. The gases are then cooled to: 1) 13.8°C.
2) 1380°C.
3) 138°C.
4) 1.38°C.
3) 138°C.
When acid gas flow rates, ambient temperatures or the atmospheric pressure change, it may be necessary to adjust the acid gas to air ratio and the acid gas bypass rate in split-flow plants. Ratios of lower than 2:1 indicate insufficient:
1) Air.
2) Hydrogen sulphide.
3) Heat.
4) All of the above.
2) Hydrogen sulphide.
The gas temperature leaving the incinerator is ________ to burn off any remaining H2S. 1) 260°C
2) 138°C
3) 538°C
4) 649°C
4) 649°C
Claus reaction temperature of 232°C is best obtained by adjusting the hot combustion products from the first pass of the sulphur boiler. The temperature of the exit gases is about 18°C higher than the inlet temperature due to the release of:
1) Atmospheric heat.
2) Exothermic heat.
3) Endothermic heat.
4) Intrinsic heat.
2) Exothermic heat.
In sulphur plants where chemical reactions are the backbone of the process, the effect of temperature on the reaction rates is important. In an operating sulphur plant, of the following, the operator is least concerned with the temperature of the: 1) Stack outlet.
2) Sulphur.
3) Condenser.
4) Tail gas.
2) Sulphur.
The sulphur purity test samples are taken from the liquid sulphur drains. The tests performed on samples from these locations determine the content of all of the following except the:
1) Sulphur plant feed gas
2) Carbon dioxide.
3) Sulphur dioxide.
4) Non-acid gas residue components.
1) Sulphur plant feed gas
nowing the amount of H2S in the sulphur plant’s acid gas is critical in setting:
1) The reaction furnace design temperature.
2) The correct air to gas ratio in the reaction furnace.
3) The correct air to gas ratio in the incinerator.
4) The amount of Hot Gas by-pass flow to the first converter.
2) The correct air to gas ratio in the reaction furnace.
Burning more than 1/3 of the H2S in the reaction furnace will increase SO2 emissions from the incinerator stack due to:
1) Insufficient H2S to react with SO2 generated.
2) An increased amount of water vapour.
3) Fouling of the catalyst.
4) Insufficient SO2 to react with H2S.
1) Insufficient H2S to react with SO2 generated.
To ensure the complete combustion of H2S and sulphur in the tail gas, the stack outlet temperature is maintained at:
1) 650°C.
2) 538°C.
3) 232°C.
4) 2325°C.
2) 538°C.
In sensitive locations and around large plants, several monitoring stations may be used. A mandatory cutback of the sulphur plant load to 50%, until the pollution levels drop is required when reported SO2 concentrations equal or exceed:
1) 10.2 ppm.
2) 20 ppm.
3) 2.0 ppm.
4) 0.20 ppm.
4) 0.20 ppm
The graph shown shows the various sulphur recovery percentages corresponding to the amount of air fed into the furnace. The upper line shows the absolute stoichiometric limit. If 6% excess air is fed into the furnace, the sulphur recovery rate would increase over the actual rate to:
1) 95%.
2) 98%.
3) 96%.
4) 97%
4) 97%
When obtaining a stock tank oil sample, the sample should be obtained from the:
1) Separator in a plastic bottle after purging the sample valve.
2) Stock tank in a plastic bottle after purging the sample valve.
3) Separator in a plastic bottle before purging the sample valve.
4) Separator in a glass bottle before purging the sample valve.
1) Separator in a plastic bottle after purging the sample valve.
Identify part E of the sampling apparatus in the illustration below:
1) Source valve
2) Purge valve
3) Vent
4) Sample line
3) Vent
When sampling sweet gas, if there is sufficient space to connect the sample cylinder directly to the sample valve using a close nipple, the sample line:
1) Is longer than 2 metres.
2) May be eliminated.
3) Is connected to the separator.
4) Is located on a dead leg.
2) May be eliminated.
Identify part A of the sampling apparatus in the illustration below:
1) Vent
2) Sample Line
3) Liquid sample cylinder position
4) Gas sample cylinder
4) Gas sample cylinder
Identify part F of the sampling apparatus in the illustration below:
1) Vent
2) Sample Line
3) Liquid sample cylinder position
4) Gas sample cylinde
3) Liquid sample cylinder position
To prevent extra lab costs for stock tank oil sample analysis, the lab must be specifically requested to analyze the stock tank sample for only:
1) Pour point, three-point viscosity and distillation.
2) Pour point, three-point viscosity and B.S.& W.
3) Density, pour point and B.S. & W.
4) Density, sulphur content and B.S. & W.
4) Density, sulphur content and B.S. & W.
For samples obtained using the Evacuated Cylinder Method, it is extremely important to take an outage before transport. 1) True 2) False
2) False
H2S content should be determined in the:
1) Lab using a GC.
2) Lab using a mass spectrometer.
3) Field using the Tutweiler method.
4) Field using a mass spectrometer.
3) Field using the Tutweiler method.
For gas, the best sample point is a valve on:
1) Top of a horizontal line close to the separator.
2) The underside of a horizontal line close to the separator.
3) The separator, upstream of any pressure-reducing valve.
4) The separator, downstream of any pressure-reducing valve.
1) Top of a horizontal line close to the separator.
When testing a new gas well, samples should be obtained early in the test:
1) Before the well flow has stabilized.
2) After the well flow has stabilized.
3) By the well testing contractor.
4) By a new employee.
2) After the well flow has stabilized.
For samples from a process flow where a low-pressure, second-stage separator is used and the gas is measured, why is it recommended that Cycle/Purge Method be used to obtain the duplicate samples?
1) Because a sample could be contaminated by air when using the Brine Displacement Method.
2) A water sample should be obtained in a plastic bottle from the separator.
3) Because the H2S content must be determined in the field using the Tutweiler Method.
4) Because a sample could be contaminated by air when the Evacuated Cylinder Method is used.
4) Because a sample could be contaminated by air when the Evacuated Cylinder Method is used.
Pressurized samples may be transported in:
1) Commercial aircraft.
2) Public transport.
3) Company vehicles.
4) Company aircraft
3) Company vehicles.
A gas stream separator must be able to cause a __________ of liquid hydrocarbons.
1) change in flow direction
2) pressure reduction
3) primary-phase separation
4) increase in temperature
3) primary-phase separation
The principle utilized in separation that is used to accelerate separation by throwing the heavier components to the outside and away from the lighter gases is:
1) Absorption.
2) Force of gravity.
3) Impingement.
4) Centrifugal force
4) Centrifugal force
It is more efficient to pump gas-free liquids to a storage area because flash vapour problems can result during pumping and vapour losses from storage tanks are decreased dramatically.
1) True 2) False
1) True
Condensation is:
1) A process that separates a mixture according to dew points.
2) A process that separates a mixture according to weights.
3) A process that separates a mixture according to boiling points.
4) A process that separates a mixture according to solubilities.
1) A process that separates a mixture according to dew points.
Absorption is:
1) A process that separates a mixture according to boiling points.
2) A process that separates a mixture according to solubilities.
3) A process that separates a mixture according to dew points.
4) A process that separates a mixture according to weights.
2) A process that separates a mixture according to solubilities.
The principle utilized in separation that causes heavier components to disengage from the stream by
directing flowing gas against a surface, thus changing its motion is referred to as:
1) Centrifugal force.
2) Impingement.
3) Absorption.
4) Filtration.
2) Impingement.
The force of gravity, distillation, centrifugal force, adsorption and impingement are all principles that may be
used to design separators and achieve complete separation of liquid from gases.
1) True
2) False
2) False
Gas expansion improves liquid separation due to:
1) A corresponding drop in temperature will also occur.
2) Gas density is decreased.
3) A corresponding increase in temperature will also occur.
4) Gas velocity will increase.
2) Gas density is decreased.
The well stream has gone through a knockout drum and the resulting gas and liquid flow heads towards
further separation. During the operation, a hydrate forms in the out flowing pipe, slowing down the flow and the production of the well. The reason for hydrate formation is:
1) A malfunctioning knockout drum has allowed water to exit the drum.
2) The temperature of the knockout drum is too low and allowed condensation to occur.
3) Knockout drums only remove free water, not all water from the system.
4) The knockout drum is allowing particulate matter to flow through the
drum.
3) Knockout drums only remove free water, not all water from the system.
You are engineering a separator upstream of a gas compressor. Of those listed below, the most suitable
design would be:
1) Free Water Knockout
2) Horizontal Separator
3) Vertical Separator with a Demister Pad
4) Scrubber
4) Scrubber
The design principle used in a Mist Extractor is:
1) Liquid retention time.
2) Gas velocity.
3) Stream temperature and pressure.
4) Liquid impingement.
4) Liquid impingement.
A scrubber is a separator designed to handle gas streams with:
1) Heavy solids content.
2) Small liquid content.
3) Heavy liquids content.
4) High concentrations of H2S.
2) Small liquid content.
The factor in the separation of liquids and gases that affects the viscosity of the fluid and, therefore, its velocity and flow is: 1) Gas velocity. 2) Volume. 3) Gas temperature. 4) Gas pressure.
3) Gas temperature.
The amount of water a gas is capable of absorbing before it becomes “saturated” is dependent upon:
1) Gas Temperature.
2) Gas Velocity.
3) Amount of solids in the gas.
4) Whether free water is present.
1) Gas Temperature.
Settling is:
1) A process that separates a mixture according to dew points.
2) A process that separates a mixture according to boiling points.
3) A process that separates a mixture according to solubilities.
4) A process that separates a mixture according to weights.
4) A process that separates a mixture according to weights.
A drip may be provided near a well for the removal of:
1) Traces of water, gasoline or oil.
2) Entrained liquids by filtration.
3) Heavy solids content.
4) Condensed fine particles from a gas stream.
1) Traces of water, gasoline or oil.
A total liquids knockout vessel is designed to:
1) Handle gas streams with small liquid content.
2) Remove entrained liquids by filtration.
3) Remove liquids from high-pressure gas streams.
4) Remove traces of water, oil and gasoline.
3) Remove liquids from high-pressure gas streams
A scrubber:
1) Is designed to handle gas streams with small liquid content.
2) Is usually installed upstream of compressors.
3) Is designed to remove entrained fine particles from a gas stream.
4) All of the above.
4) All of the above.
The factor in the separation of liquids and gases that affects the gas composition and the amount of liquids removed from the stream is: 1) Gas temperature. 2) Gas pressure. 3) Gas expansion. 4) Retention time.
2) Gas pressure.
A mist extractor is a separating device that removes entrained liquid and particles by:
1) Force of gravity.
2) Distillation.
3) Filtration or adsorption in depth.
4) Filtration or impingement in depth.
Filtration or impingement in depth
One reason for separating liquids from gases is that:
1) Measurement of gases and liquids separately is required for accuracy.
2) Hydrate formation can be prevented by increasing water content.
3) Hydrocarbons occur only in a gas state.
4) Hydrocarbons occur only in a liquid state.
1) Measurement of gases and liquids separately is required for accuracy.
Fractional distillation is:
1) A process that separates a mixture according to weights.
2) A process that separates a mixture according to solubilities.
3) A process that separates a mixture according to boiling points.
4) A process that separates a mixture according to dew points.
3) A process that separates a mixture according to boiling points.