US20180334621A1 - Crude hydrocarbon fluids demulsification system - Google Patents
Crude hydrocarbon fluids demulsification system Download PDFInfo
- Publication number
- US20180334621A1 US20180334621A1 US15/601,491 US201715601491A US2018334621A1 US 20180334621 A1 US20180334621 A1 US 20180334621A1 US 201715601491 A US201715601491 A US 201715601491A US 2018334621 A1 US2018334621 A1 US 2018334621A1
- Authority
- US
- United States
- Prior art keywords
- fluid
- heating coils
- pipe
- process fluid
- separator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/06—Dewatering or demulsification of hydrocarbon oils with mechanical means, e.g. by filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/042—Breaking emulsions by changing the temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/12—Auxiliary equipment particularly adapted for use with liquid-separating apparatus, e.g. control circuits
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/08—Controlling or regulating
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B3/00—Ohmic-resistance heating
- H05B3/78—Heating arrangements specially adapted for immersion heating
- H05B3/82—Fixedly-mounted immersion heaters
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B2203/00—Aspects relating to Ohmic resistive heating covered by group H05B3/00
- H05B2203/021—Heaters specially adapted for heating liquids
Definitions
- This disclosure relates to the demulsification of multiphase fluids, for example, fluids flowing through flowlines in a hydrocarbon processing facility.
- This disclosure describes technologies relating to a crude demulsification system.
- An elongate, horizontally level, pipe includes a circumferential wall.
- the pipe flows, within the circumferential wall, process fluid that includes a first fluid and a second fluid immiscible with the first fluid.
- the first fluid and the second fluid are separated by an interfacial layer.
- Heating coils are disposed within the pipe. Each heating coil passes through an interior region of the pipe between the circumferential wall at a respective height from a bottom of the pipe.
- the heating coils generate heat.
- a controller is connected to the heating coils.
- the controller triggers at least one of the heating coils that is nearest to a location of the interfacial layer within the interior region to apply heat to the interfacial layer.
- the heat is sufficient to at least partially demulsify the interfacial layer.
- the heating coils pass through the interior region of the pipe between the circumferential wall at different heights along an entire axial length of the pipe.
- the heating coils can include an electrical heating coil and an electrical power supply.
- the heating coils can include a first heating coil passing through the interior region at a first height from the bottom of the pipe that is substantially one-third of a radius of the pipe, a second heating coil passing through the interior region at a second height from the bottom of the pipe that is substantially one-half of the radius of the pipe.
- Each of the heating coils can be encased in a protective and heat-conductive sheath configured to protect the heating coils.
- the process fluid can include water and hydrocarbon liquids.
- the heat generated by the heating coils is sufficient to at least partially demulsify the water and hydrocarbon liquids.
- a separator with a separator inlet is fluidically coupled to an outlet of the pipe.
- the separator receives the fluid with a heated interfacial layer at the separator inlet.
- a demulsifier can at least partially demulsify the interfacial layer.
- a demulsifier inlet can receive the demulsifier.
- the demulsifier inlet can be positioned on the pipe.
- a process fluid comprising a first fluid and a second fluid immiscible with the first fluid is received in a flowline.
- the first fluid and the second fluid are separated by an interfacial emulsion layer.
- the flowline includes heating coils. Each heating coil passes through an interior region of a pipe between a circumferential wall at a respective height from a bottom of the pipe.
- the heating coils generate heat.
- at least one of the plurality of heating coils within a pre-heater is selectively triggered to heat the interfacial layer based at a height of the interfacial layer from the bottom of the pipe.
- the process fluid can include water and hydrocarbons.
- the process fluid is at least partially demulsified in response to applying heat to the interface height of the process fluid.
- Each of the heating coils can be positioned at a different height within the pre-heater.
- the heating coils can include an electrical heating coil.
- the heating coils include two heating coils.
- the process fluid is sent from the pre-heater to a separator.
- the process fluid can be further demulsified within the separator.
- the process fluid is demulsified within the separator using demulsifying chemicals, electrostatic grids, ultrasonics, or sand jetting.
- a process fluid receiving by a pre-heater One or more heating coils are selecting to power from out of a set of heating coils. Heat is applied to an interface of the process fluid by a selected heating coil. the process fluid is at least partially demulsified in response to applying heat to an interface height of the process fluid. The process fluid is sent from the pre-heater to a separator. The process fluid is further demulsified within the separator.
- FIG. 1 is a side cross-sectional schematic diagram of a separator with an inlet pre-heater.
- FIGS. 2A-2B show detailed cross-sectional views of the inlet pre-heater.
- FIGS. 2C-2D show detailed cross-sectional views of the inlet pre-heater.
- FIGS. 2E-2F show detailed cross-sectional views of the inlet pre-heater.
- FIGS. 2G-2H show detailed cross-sectional views of the inlet pre-heater.
- FIGS. 2I-2J show detailed cross-sectional views of the inlet pre-heater
- FIG. 3 is a flowchart showing an example method for at least partially demulsifying a fluid.
- crude-oil When producing and processing hydrocarbons, for example, crude-oil, water is often emulsified within crude-oil and should be separated from the crude-oil before being transported through pipelines to separate facilities. That is, the crude-oil must be dried or dehydrated. A low-water content in the crude-oil is essential for crude-oil transportation, particularly in pipelines, as to prevent hydrate formation. Many pipeline companies have specifications limiting the allowable amount of water within crude-oil to prevent such a hydrate formation from occurring within the pipeline. Dry crude-oil can also be less corrosive than wet crude-oil and can be easier to process in refining operations. For example, crude fluid can be produced on an off-shore platform. That is, crude-fluid is produced from a completed production well.
- the crude-oil from the crude-fluid produced on the off-shore platform Before the crude-oil from the crude-fluid produced on the off-shore platform can be transported to a refinery onshore, the crude-oil must be sufficiently dehydrated. Proper separation, demulsion, and dehydration can take place on the offshore platform before the dehydrated crude-oil enters the pipeline. In winter months, when the ambient temperature is lower, demulsifying the crude oil can become more difficult. The lower ambient temperatures can create bottlenecks in processing plants due to increased retention times necessary to separate the water from the oil.
- This disclosure describes partially demulsifying and separating water that has emulsified into oil before the fluid has entered the separator.
- the separation is achieved by applying heat with a pre-heater to an interface layer between the water and the oil within the flowline upstream of the separator to initiate and accelerate the demulsification and separation process.
- the targeted heating is more effective and requires less energy than traditional demulsification and separation methods.
- the in-line separator can consume 20% of the power used by a separator.
- FIG. 1 shows a flowline fluid demulsification and separation system 100 that is capable of separating and demulsifying water and crude-oil or water and other hydrocarbon liquids, such as condensate.
- the separation system 100 can be located in any production or refining facility that processes crude-fluids.
- the crude-fluid can be from a wellbore, an upstream separator, or an upstream facility.
- the separation system 100 includes a flowline 122 through which a process fluid 102 flows.
- the process fluid 102 can include crude fluids including water and crude-oil.
- a flowline such as flowline 122 , transports fluid between different sections of a single facility while pipelines transport fluid between different facilities.
- the flowline 122 is an elongate, substantially horizontally level, pipe with a circumferential wall 130 .
- the flowline 122 can be sufficiently level to allow for a consistent emulsion layer to form within the flowline 122 .
- the process fluid 102 flows, within the circumferential wall, a process fluid 102 that includes a first fluid and a second fluid immiscible with the first fluid.
- Such fluids can include water and hydrocarbon liquids, such as crude-oil.
- the process fluid 102 can include gas as well.
- the first fluid and the second fluid are separated by an interfacial layer 132 .
- the flowline 122 can be of sufficient length to allow bulk separation to occur within the flowline 122 . That is, an upper portion of the flowline 122 is filled predominantly with crude-oil and a lower portion of the flowline 122 is filled predominantly filled with water with an emulsion layer in between the two portions.
- the pre-heater 104 can include heating coils, such as heating coils 202 ( FIGS. 2A-2D ) that generate heat; the heating coils can be disposed within a pipe.
- the heating coils can be placed at a height approximately equal to the interfacial layer 131 to specifically heat the emulsion layer and to at least partially demulsify the process fluid 102 . If electrical heating coils are used, they can be made of any heating coil material, such as nichrome.
- a controller 128 can be connected to the heating coils.
- the controller 128 can trigger at least one of the heating coils that is nearest to the location of the interfacial layer 131 within the interior region or the pre-heater 104 to apply heat to the interfacial layer 131 .
- the targeted application of heat is sufficient to at least partially demulsify the heated interfacial layer 131 .
- a demulsifier 126 (a chemical designed to demulsify process fluid) can be injected into either the pre-heater or the separator 108 .
- FIGS. 2A-2B show a side cut-away view and a front view of an example pre-heater 104 , respectively.
- the pre-heater 104 can include heating coils 202 positioned at a set height along the pre-heater 104 .
- the heating coils 202 passes through an interior region of the pipe between the circumferential wall 130 at a respective height from a bottom of the pipe. The height is set to match the height of the interface level within the pre-heater 104 .
- the heating coils 202 can pass through the interior region of the pipe along an entire axial length of the pre-heater 104 .
- the length of the heater coils can be dependent upon the diameter of the flowline.
- the heating coils 202 are encased in a protective and heat-conductive sheath 204 that protects the heating coils 202 from the process fluid 102 .
- the protective sheaths 204 protect the heating coils 202 from the process fluid 102 .
- the sheaths 204 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline.
- FIGS. 2C-2D show a side cut-away view and a front view of an example pre-heater 104 , respectively.
- the pre-heater 104 can include multiple layers of heating coils 202 positioned at different heights.
- each heating coil 202 passes through an interior region of the pipe between the circumferential wall 130 at a respective height from a bottom of the pipe.
- the varying heights allow individual coils to be used in the event of a process upset or slugging event; such an event can affect the height of the interface level within the pre-heater 104 .
- FIGS. 1 such as the implementation illustrated in FIGS.
- the heating coils 202 can pass through the interior region of the pipe along an entire axial length of the pre-heater 104 .
- the heating coils 202 can extend only partially along the length of the pre-heater 104 .
- the pre-heater 104 can include two heater coils 202 : a first heating coil 202 a and a second heating coil 202 b. In some implementations, more than two heating coils can be used.
- the first heating coil 202 a passes through the interior region at a first height from the bottom of the pipe that is substantially one-third of a radius of the pipe, and the second heating coil 202 b passes through the interior region at a second height from the bottom of the pipe that is substantially one-half of the radius of the pipe.
- Each of the heating coils 202 is encased in a protective and heat-conductive sheath 204 that protects the heating coils 202 from the process fluid 102 .
- the first heating coil 202 a is encased in a first protective sheath 204 a while the second heating coil 202 b is encased in a second protective sheath 204 b.
- the protective sheaths 204 protect the heating coils 202 from the process fluid 102 .
- the sheaths 204 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline.
- FIGS. 2E-2F show a side cut-away view and a front view of an example pre-heater 104 .
- the pre-heater 104 can include heating coils 210 .
- the heating coils 202 can pass through the interior region of the pipe laterally across the pre-heater 104 .
- the heating coils 210 can be encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from the process fluid 102 .
- the sheath 212 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline.
- FIGS. 2G-2H show a side cut-away view and a front view of an example pre-heater 104 .
- the pre-heater 104 can include multiple heating coils 210 positioned at different heights.
- each heating coil 210 passes through an interior region of the pipe between the circumferential wall 130 at a respective height from a bottom of the pipe.
- the varying heights allow individual coils to be used in the event of a process upset or slugging event; such an event can affect the height of the interface level within the pre-heater 104 .
- FIGS. 1 such as the implementation illustrated in FIGS.
- the heating coils 210 can pass through the interior region of the pipe laterally across the pre-heater 104 .
- the pre-heater 104 can include multiple heater coils 210 : a first heating coil 210 a and a second heating coil 210 b.
- Each of the heating coils 210 can be encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from the process fluid 102 .
- the first heating coil 210 a is encased in a first protective sheath 212 a while the second heating coil 210 b is encased in a second protective sheath 212 b.
- the protective sheaths 212 protect the heating coils 210 from the process fluid 102 .
- the sheaths 212 a and 212 b can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline.
- FIGS. 2I-2J show a side cut-away view and a front view of an example pre-heater 104 .
- the pre-heater 104 can include multiple heating coils 210 .
- the heating coils 202 can pass through the interior region of the pipe laterally across the pre-heater 104 .
- the pre-heater 104 can include multiple heater coils 210 : a first heating coil 210 a, a second heating coil 210 b, and a third heating coil 210 c.
- each of the heating coils 210 is positioned at the same height along the length of the pre-heater.
- Each of the heating coils 210 is encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from the process fluid 102 .
- the first heating coil 210 a is encased in a first protective sheath 212 a
- the second heating coil 210 b is encased in a protective sheath 212 b
- the third heating coil 210 c is encased in a third protective sheath 212 c.
- the heating coils can include an electrical heating coil.
- an electrical power supply 206 provides current to heat up at least one of the heating coils 202 or heating coils 210 .
- different numbers heating coils 210 can be activated based on a temperature of a process fluid 102 .
- a sensor can send a signal to a controller. The controller then activates the necessary number of coils based on the desired load.
- the heating coils 202 or 210 can include coiled tubing through which heat media can be flowed to heat up the heating coils 202 or 210 .
- a heat media pump flows the heat media through the heating coils and a temperature regulator controls the temperature of the heat media fluid.
- a separator 108 can be positioned downstream of the pre-heater 104 .
- the separator 108 has a separator inlet 124 that is fluidically coupled to an outlet 124 of the pre-heater 104 .
- the separator inlet 124 and the pre-heater outlet 124 can be the same opening.
- the separator 108 receives the process fluid 102 that has had the interfacial layer 132 heated by the pre-heater 104 prior to entering the separator 108 .
- As the process fluid 102 enters the separator it can hit a deflector plate 106 .
- the deflector plate helps release entrapped gasses from the process fluid and confines turbulent fluid flow to one end of the separator.
- a different inlet can be used.
- a spreader inlet can be used.
- the process fluid 102 further separates into an upper layer of oil 120 and a lower layer of water 118 .
- the separator 108 can contain a demulsion apparatus 116 that can further separate and demulsify the process fluid 102 .
- Such a demulsion apparatus can include demulsifying chemicals, electrostatic grids, ultrasonic emitters, sand jets, heaters or any other apparatus that can further demulsify the process fluid.
- the oil phase is directed into an oil bucket 110 and out an oil outlet 112 to either further refining or a pipeline while the water 118 phase is directed out the bottom water outlet 114 where the water can be cleaned and released to the environment.
- FIG. 3 is a flowchart showing a method 300 for partially demulsifying a process fluid prior to the process fluid entering the separator.
- process fluid that include a first fluid and a second fluid immiscible with the first fluid is received in a flowline.
- the first fluid and the second fluid are separated by an interfacial emulsion layer.
- the height of the interfacial emulsion layer from the bottom of the pipe can be determined, and at 304 at least one of the plurality of heating coils is selectively triggered to heat the interfacial layer 132 based on a height of the interfacial layer 131 from the bottom of the pipe.
- the heating coil can be selected manually by an operator.
- Each of the plurality of heating coils can be positioned at a different height within the pre-heater.
- the process fluid is at least partially demulsified in response to applying heat to the interface height of the process fluid.
- the process fluid is sent to a separator where the process fluid can be further demulsified.
- Demulsifying the process fluid within the separator can involve using demulsifying chemicals, electrostatic grids, ultrasonics, sand jetting, or any other apparatus or method to demulsify the process fluid.
Abstract
Description
- This disclosure relates to the demulsification of multiphase fluids, for example, fluids flowing through flowlines in a hydrocarbon processing facility.
- When processing crude fluids during hydrocarbon production, hydrocarbon liquids and water become emulsified within one another. The two liquids are separated to meet refining and pipeline specifications. Separation can be done using gravity separation and retention time, demulsification chemicals, or other methods. Flowlines are used to transport crude fluids from one processing stage to another within a refining or production plant. Once the crude fluid is refined and processed, it can be transported through a pipeline that connects a production or production facility to a separate facility.
- This disclosure describes technologies relating to a crude demulsification system.
- An example implementation of the subject matter described within this disclosure is a flowline fluid demulsification system with the following features. An elongate, horizontally level, pipe includes a circumferential wall. The pipe flows, within the circumferential wall, process fluid that includes a first fluid and a second fluid immiscible with the first fluid. The first fluid and the second fluid are separated by an interfacial layer. Heating coils are disposed within the pipe. Each heating coil passes through an interior region of the pipe between the circumferential wall at a respective height from a bottom of the pipe. The heating coils generate heat. A controller is connected to the heating coils. The controller triggers at least one of the heating coils that is nearest to a location of the interfacial layer within the interior region to apply heat to the interfacial layer. The heat is sufficient to at least partially demulsify the interfacial layer.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. The heating coils pass through the interior region of the pipe between the circumferential wall at different heights along an entire axial length of the pipe.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. The heating coils can include an electrical heating coil and an electrical power supply.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. The heating coils can include a first heating coil passing through the interior region at a first height from the bottom of the pipe that is substantially one-third of a radius of the pipe, a second heating coil passing through the interior region at a second height from the bottom of the pipe that is substantially one-half of the radius of the pipe.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. Each of the heating coils can be encased in a protective and heat-conductive sheath configured to protect the heating coils.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. The process fluid can include water and hydrocarbon liquids. The heat generated by the heating coils is sufficient to at least partially demulsify the water and hydrocarbon liquids.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. A separator with a separator inlet is fluidically coupled to an outlet of the pipe. The separator receives the fluid with a heated interfacial layer at the separator inlet.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. A demulsifier can at least partially demulsify the interfacial layer. A demulsifier inlet can receive the demulsifier.
- Aspects of the example implementation, which can be combined with the example implementation alone or in combination, include the following. The demulsifier inlet can be positioned on the pipe.
- An example implementation of the subject matter described within this disclosure is a method with the following features. A process fluid comprising a first fluid and a second fluid immiscible with the first fluid is received in a flowline. The first fluid and the second fluid are separated by an interfacial emulsion layer. The flowline includes heating coils. Each heating coil passes through an interior region of a pipe between a circumferential wall at a respective height from a bottom of the pipe. The heating coils generate heat. at least one of the plurality of heating coils within a pre-heater is selectively triggered to heat the interfacial layer based at a height of the interfacial layer from the bottom of the pipe.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. The process fluid can include water and hydrocarbons.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. the process fluid is at least partially demulsified in response to applying heat to the interface height of the process fluid.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. Each of the heating coils can be positioned at a different height within the pre-heater.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. The heating coils can include an electrical heating coil.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. The heating coils include two heating coils.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. the process fluid is sent from the pre-heater to a separator.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. The process fluid can be further demulsified within the separator.
- Aspects of the example method, which can be combined with the example method alone or in combination, include the following. The process fluid is demulsified within the separator using demulsifying chemicals, electrostatic grids, ultrasonics, or sand jetting.
- An example implementation of the subject matter described within this disclosure is a method with the following features. A process fluid receiving by a pre-heater. One or more heating coils are selecting to power from out of a set of heating coils. Heat is applied to an interface of the process fluid by a selected heating coil. the process fluid is at least partially demulsified in response to applying heat to an interface height of the process fluid. The process fluid is sent from the pre-heater to a separator. The process fluid is further demulsified within the separator.
- The details of one or more implementations of the subject matter described in this specification are set forth in the accompanying drawings and the description that follows. Other features, aspects, and advantages of the subject matter will become apparent from the description, the drawings, and the claims.
-
FIG. 1 is a side cross-sectional schematic diagram of a separator with an inlet pre-heater. -
FIGS. 2A-2B show detailed cross-sectional views of the inlet pre-heater. -
FIGS. 2C-2D show detailed cross-sectional views of the inlet pre-heater. -
FIGS. 2E-2F show detailed cross-sectional views of the inlet pre-heater. -
FIGS. 2G-2H show detailed cross-sectional views of the inlet pre-heater. -
FIGS. 2I-2J show detailed cross-sectional views of the inlet pre-heater -
FIG. 3 is a flowchart showing an example method for at least partially demulsifying a fluid. - Like reference numbers and designations in the various drawings indicate like elements.
- When producing and processing hydrocarbons, for example, crude-oil, water is often emulsified within crude-oil and should be separated from the crude-oil before being transported through pipelines to separate facilities. That is, the crude-oil must be dried or dehydrated. A low-water content in the crude-oil is essential for crude-oil transportation, particularly in pipelines, as to prevent hydrate formation. Many pipeline companies have specifications limiting the allowable amount of water within crude-oil to prevent such a hydrate formation from occurring within the pipeline. Dry crude-oil can also be less corrosive than wet crude-oil and can be easier to process in refining operations. For example, crude fluid can be produced on an off-shore platform. That is, crude-fluid is produced from a completed production well. Before the crude-oil from the crude-fluid produced on the off-shore platform can be transported to a refinery onshore, the crude-oil must be sufficiently dehydrated. Proper separation, demulsion, and dehydration can take place on the offshore platform before the dehydrated crude-oil enters the pipeline. In winter months, when the ambient temperature is lower, demulsifying the crude oil can become more difficult. The lower ambient temperatures can create bottlenecks in processing plants due to increased retention times necessary to separate the water from the oil.
- There are several ways to separate water that has been emulsified in oil, such as gravity separation, demulsifying chemicals, electrostatic grids, and many others. All of these methods involve a bulk of the separation taking place within a large separator or pressure vessel. Such large quantities of fluid can take a substantial amount of time and energy to fully demulsify and separate.
- This disclosure describes partially demulsifying and separating water that has emulsified into oil before the fluid has entered the separator. The separation is achieved by applying heat with a pre-heater to an interface layer between the water and the oil within the flowline upstream of the separator to initiate and accelerate the demulsification and separation process. The targeted heating is more effective and requires less energy than traditional demulsification and separation methods. For example, the in-line separator can consume 20% of the power used by a separator.
-
FIG. 1 shows a flowline fluid demulsification andseparation system 100 that is capable of separating and demulsifying water and crude-oil or water and other hydrocarbon liquids, such as condensate. Theseparation system 100 can be located in any production or refining facility that processes crude-fluids. In some implementations, the crude-fluid can be from a wellbore, an upstream separator, or an upstream facility. Theseparation system 100 includes aflowline 122 through which aprocess fluid 102 flows. Theprocess fluid 102 can include crude fluids including water and crude-oil. In the context of this disclosure, a flowline, such asflowline 122, transports fluid between different sections of a single facility while pipelines transport fluid between different facilities. Theflowline 122 is an elongate, substantially horizontally level, pipe with acircumferential wall 130. Theflowline 122 can be sufficiently level to allow for a consistent emulsion layer to form within theflowline 122. Theprocess fluid 102 flows, within the circumferential wall, aprocess fluid 102 that includes a first fluid and a second fluid immiscible with the first fluid. Such fluids can include water and hydrocarbon liquids, such as crude-oil. In some implementations, theprocess fluid 102 can include gas as well. The first fluid and the second fluid are separated by aninterfacial layer 132. Theflowline 122 can be of sufficient length to allow bulk separation to occur within theflowline 122. That is, an upper portion of theflowline 122 is filled predominantly with crude-oil and a lower portion of theflowline 122 is filled predominantly filled with water with an emulsion layer in between the two portions. - Downstream of the
flowline 122 is a pre-heater 104. The pre-heater 104 can include heating coils, such as heating coils 202 (FIGS. 2A-2D ) that generate heat; the heating coils can be disposed within a pipe. The heating coils can be placed at a height approximately equal to theinterfacial layer 131 to specifically heat the emulsion layer and to at least partially demulsify theprocess fluid 102. If electrical heating coils are used, they can be made of any heating coil material, such as nichrome. To regulate the pre-heater 104, acontroller 128 can be connected to the heating coils. Thecontroller 128 can trigger at least one of the heating coils that is nearest to the location of theinterfacial layer 131 within the interior region or the pre-heater 104 to apply heat to theinterfacial layer 131. The targeted application of heat is sufficient to at least partially demulsify the heatedinterfacial layer 131. In some implementations, a demulsifier 126 (a chemical designed to demulsify process fluid) can be injected into either the pre-heater or theseparator 108. -
FIGS. 2A-2B show a side cut-away view and a front view of anexample pre-heater 104, respectively. In some implementations, the pre-heater 104 can includeheating coils 202 positioned at a set height along thepre-heater 104. In other words, the heating coils 202 passes through an interior region of the pipe between thecircumferential wall 130 at a respective height from a bottom of the pipe. The height is set to match the height of the interface level within thepre-heater 104. In some implementations, such as the implementation illustrated inFIGS. 2A and 2B , the heating coils 202 can pass through the interior region of the pipe along an entire axial length of the pre-heater 104. The length of the heater coils can be dependent upon the diameter of the flowline. The heating coils 202 are encased in a protective and heat-conductive sheath 204 that protects the heating coils 202 from theprocess fluid 102. Theprotective sheaths 204 protect the heating coils 202 from theprocess fluid 102. Thesheaths 204 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline. -
FIGS. 2C-2D show a side cut-away view and a front view of anexample pre-heater 104, respectively. In some implementations, the pre-heater 104 can include multiple layers ofheating coils 202 positioned at different heights. In other words, eachheating coil 202 passes through an interior region of the pipe between thecircumferential wall 130 at a respective height from a bottom of the pipe. The varying heights allow individual coils to be used in the event of a process upset or slugging event; such an event can affect the height of the interface level within thepre-heater 104. In some implementations, such as the implementation illustrated inFIGS. 2C and 2D , the heating coils 202 can pass through the interior region of the pipe along an entire axial length of the pre-heater 104. In some implementations, the heating coils 202 can extend only partially along the length of the pre-heater 104. The pre-heater 104 can include two heater coils 202: afirst heating coil 202 a and asecond heating coil 202 b. In some implementations, more than two heating coils can be used. Thefirst heating coil 202 a passes through the interior region at a first height from the bottom of the pipe that is substantially one-third of a radius of the pipe, and thesecond heating coil 202 b passes through the interior region at a second height from the bottom of the pipe that is substantially one-half of the radius of the pipe. Each of the heating coils 202 is encased in a protective and heat-conductive sheath 204 that protects the heating coils 202 from theprocess fluid 102. Thefirst heating coil 202 a is encased in a firstprotective sheath 204 a while thesecond heating coil 202 b is encased in a secondprotective sheath 204 b. Theprotective sheaths 204 protect the heating coils 202 from theprocess fluid 102. Thesheaths 204 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline. -
FIGS. 2E-2F show a side cut-away view and a front view of anexample pre-heater 104. In some implementations, the pre-heater 104 can include heating coils 210. In some implementations, such as the implementation illustrated inFIGS. 2E and 2F , the heating coils 202 can pass through the interior region of the pipe laterally across thepre-heater 104. The heating coils 210 can be encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from theprocess fluid 102. Thesheath 212 can be made of metal, ceramic, or any other material suitable to protect heating coils in a flowline. -
FIGS. 2G-2H show a side cut-away view and a front view of anexample pre-heater 104. In some implementations, the pre-heater 104 can includemultiple heating coils 210 positioned at different heights. In other words, eachheating coil 210 passes through an interior region of the pipe between thecircumferential wall 130 at a respective height from a bottom of the pipe. The varying heights allow individual coils to be used in the event of a process upset or slugging event; such an event can affect the height of the interface level within thepre-heater 104. In some implementations, such as the implementation illustrated inFIGS. 2G and 2H , the heating coils 210 can pass through the interior region of the pipe laterally across thepre-heater 104. The pre-heater 104 can include multiple heater coils 210: afirst heating coil 210 a and asecond heating coil 210 b. Each of the heating coils 210 can be encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from theprocess fluid 102. Thefirst heating coil 210 a is encased in a firstprotective sheath 212 a while thesecond heating coil 210 b is encased in a secondprotective sheath 212 b. Theprotective sheaths 212 protect the heating coils 210 from theprocess fluid 102. Thesheaths -
FIGS. 2I-2J show a side cut-away view and a front view of anexample pre-heater 104. In some implementations, the pre-heater 104 can include multiple heating coils 210. In some implementations, such as the implementation illustrated inFIGS. 2I and 2J , the heating coils 202 can pass through the interior region of the pipe laterally across thepre-heater 104. The pre-heater 104 can include multiple heater coils 210: afirst heating coil 210 a, asecond heating coil 210 b, and athird heating coil 210 c. In this implementations, each of the heating coils 210 is positioned at the same height along the length of the pre-heater. Each of the heating coils 210 is encased in a protective and heat-conductive sheath 212 that protects the heating coils 210 from theprocess fluid 102. Thefirst heating coil 210 a is encased in a firstprotective sheath 212 a, thesecond heating coil 210 b is encased in aprotective sheath 212 b, and thethird heating coil 210 c is encased in a thirdprotective sheath 212 c. - In some implementations, the heating coils, such as heating coils 202 or
heating coils 210, can include an electrical heating coil. In such an implementation, anelectrical power supply 206 provides current to heat up at least one of the heating coils 202 or heating coils 210. In some implementations, different numbers heating coils 210 can be activated based on a temperature of aprocess fluid 102. In such an implementation, a sensor can send a signal to a controller. The controller then activates the necessary number of coils based on the desired load. In some implementations, the heating coils 202 or 210 can include coiled tubing through which heat media can be flowed to heat up the heating coils 202 or 210. In such an implementation, a heat media pump flows the heat media through the heating coils and a temperature regulator controls the temperature of the heat media fluid. - in some implementations, a
separator 108 can be positioned downstream of the pre-heater 104. Theseparator 108 has aseparator inlet 124 that is fluidically coupled to anoutlet 124 of the pre-heater 104. In some implementations, theseparator inlet 124 and thepre-heater outlet 124 can be the same opening. Theseparator 108 receives theprocess fluid 102 that has had theinterfacial layer 132 heated by the pre-heater 104 prior to entering theseparator 108. As theprocess fluid 102 enters the separator, it can hit adeflector plate 106. The deflector plate helps release entrapped gasses from the process fluid and confines turbulent fluid flow to one end of the separator. In some implementations, a different inlet can be used. For example, a spreader inlet can be used. Once in theseparator 108, theprocess fluid 102 further separates into an upper layer ofoil 120 and a lower layer ofwater 118. Theseparator 108 can contain ademulsion apparatus 116 that can further separate and demulsify theprocess fluid 102. Such a demulsion apparatus can include demulsifying chemicals, electrostatic grids, ultrasonic emitters, sand jets, heaters or any other apparatus that can further demulsify the process fluid. Once theprocess fluid 102 has been fully demulsified and separated intoseparate water 118 andoil 120 phases, the oil phase is directed into anoil bucket 110 and out anoil outlet 112 to either further refining or a pipeline while thewater 118 phase is directed out thebottom water outlet 114 where the water can be cleaned and released to the environment. -
FIG. 3 is a flowchart showing amethod 300 for partially demulsifying a process fluid prior to the process fluid entering the separator. At 302, process fluid that include a first fluid and a second fluid immiscible with the first fluid is received in a flowline. The first fluid and the second fluid are separated by an interfacial emulsion layer. The height of the interfacial emulsion layer from the bottom of the pipe can be determined, and at 304 at least one of the plurality of heating coils is selectively triggered to heat theinterfacial layer 132 based on a height of theinterfacial layer 131 from the bottom of the pipe. In some applications, the heating coil can be selected manually by an operator. Each of the plurality of heating coils can be positioned at a different height within the pre-heater. The process fluid is at least partially demulsified in response to applying heat to the interface height of the process fluid. After passing through the pre-heater, the process fluid is sent to a separator where the process fluid can be further demulsified. Demulsifying the process fluid within the separator can involve using demulsifying chemicals, electrostatic grids, ultrasonics, sand jetting, or any other apparatus or method to demulsify the process fluid. - Thus, particular implementations of the subject matter have been described. Other implementations are within the scope of the following claims.
Claims (19)
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15/601,491 US20180334621A1 (en) | 2017-05-22 | 2017-05-22 | Crude hydrocarbon fluids demulsification system |
PCT/US2018/033850 WO2018217719A1 (en) | 2017-05-22 | 2018-05-22 | Crude hydrocarbon fluids demulsification system |
EP18733718.3A EP3630327A1 (en) | 2017-05-22 | 2018-05-22 | Crude hydrocarbon fluids demulsification system |
CN201880034055.0A CN110678243B (en) | 2017-05-22 | 2018-05-22 | Crude hydrocarbon fluid demulsification system |
US17/208,668 US11873454B2 (en) | 2017-05-22 | 2021-03-22 | Crude hydrocarbon fluids demulsification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15/601,491 US20180334621A1 (en) | 2017-05-22 | 2017-05-22 | Crude hydrocarbon fluids demulsification system |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US17/208,668 Division US11873454B2 (en) | 2017-05-22 | 2021-03-22 | Crude hydrocarbon fluids demulsification system |
Publications (1)
Publication Number | Publication Date |
---|---|
US20180334621A1 true US20180334621A1 (en) | 2018-11-22 |
Family
ID=62713075
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/601,491 Abandoned US20180334621A1 (en) | 2017-05-22 | 2017-05-22 | Crude hydrocarbon fluids demulsification system |
US17/208,668 Active 2038-03-31 US11873454B2 (en) | 2017-05-22 | 2021-03-22 | Crude hydrocarbon fluids demulsification system |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US17/208,668 Active 2038-03-31 US11873454B2 (en) | 2017-05-22 | 2021-03-22 | Crude hydrocarbon fluids demulsification system |
Country Status (4)
Country | Link |
---|---|
US (2) | US20180334621A1 (en) |
EP (1) | EP3630327A1 (en) |
CN (1) | CN110678243B (en) |
WO (1) | WO2018217719A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113620486A (en) * | 2021-08-23 | 2021-11-09 | 塔里木大学 | Organic chemistry experiment sewage treatment plant |
CN115445248A (en) * | 2022-09-16 | 2022-12-09 | 江苏理工学院 | Efficient sump oil treatment device integrating multiple demulsification technologies and treatment method thereof |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1405119A (en) * | 1918-02-06 | 1922-01-31 | Petroleum Rectifying Co | Apparatus for dehydrating petroleum emulsions |
US2547190A (en) * | 1946-01-23 | 1951-04-03 | Maloney Crawford Tank And Mfg | Oil and gas separator |
US3098827A (en) * | 1958-03-31 | 1963-07-23 | Nalco Chemical Co | Demulsification of petroleum oil emulsions |
US20020015585A1 (en) * | 2000-06-09 | 2002-02-07 | Emerson Electric Company | Multivariable compact electric heater |
US20090107558A1 (en) * | 2007-10-23 | 2009-04-30 | Quigley Peter A | Heated pipe and methods of transporting viscous fluid |
WO2010134822A1 (en) * | 2009-05-22 | 2010-11-25 | Aker Process Systems As | Method and apparatus for breaking a stable emulsion |
US20170254564A1 (en) * | 2016-03-02 | 2017-09-07 | Watlow Electric Manufacturing Company | Heater bundle for adaptive control |
Family Cites Families (48)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1612557A (en) * | 1923-09-26 | 1926-12-28 | Edwin C Weisgerber | Oil and water separator |
US2601904A (en) | 1946-12-03 | 1952-07-01 | Salt Water Control Inc | Method and apparatus for treating crude oil emulsions from oil wells |
US2730240A (en) | 1952-02-08 | 1956-01-10 | Union Oil Co | Dehydration of oils |
US3318448A (en) * | 1963-09-06 | 1967-05-09 | William E Fryer | Fluid separating and cleaning method and apparatus |
US3488294A (en) | 1966-01-17 | 1970-01-06 | Petrolite Corp | Process of inhibiting corrosion of ferrous metals and alloys employing a polyvinyl heterocyclic polymer |
US4226689A (en) | 1979-05-29 | 1980-10-07 | Petrolite Corporation | Apparatus and process for electrically resolving emulsions |
US4252631A (en) | 1980-01-09 | 1981-02-24 | The United States Of America As Represented By The United States Department Of Energy | Electrostatic coalescence system with independent AC and DC hydrophilic electrodes |
US4415426A (en) | 1980-09-30 | 1983-11-15 | Exxon Research And Engineering Co. | Electrodes for electrical coalescense of liquid emulsions |
EP0072628A1 (en) | 1981-07-27 | 1983-02-23 | Exxon Research And Engineering Company | Electrically coalescing multi-component liquid mixtures |
US4419200A (en) | 1981-07-27 | 1983-12-06 | Exxon Research And Engineering Co. | Electrical coalescense of liquid emulsions |
US4582629A (en) | 1982-03-29 | 1986-04-15 | Conoco Inc. | Use of microwave radiation in separating emulsions and dispersions of hydrocarbons and water |
US4581112A (en) | 1985-04-11 | 1986-04-08 | Exxon Research And Engineering Co. | Method and apparatus for separating wax/water from hydrocarbon mixture boiling in the lubricating oil range |
US4996490A (en) | 1986-11-18 | 1991-02-26 | Atlantic Richfield Company | Microwave apparatus and method for measuring fluid mixtures |
US5147562A (en) | 1990-12-17 | 1992-09-15 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Acoustophoresis method and apparatus |
DE4138763A1 (en) | 1991-11-26 | 1993-05-27 | Basf Ag | USE OF HOMO- OR COPOLYMERISATS BASED ON QUATERNIZED 1-VINYLIMIDAZOLES AS ORGANIC POLYELECTROLYTE |
GB9213198D0 (en) | 1992-06-22 | 1992-08-05 | Univ Cardiff | Phase partition separation method |
US5885424A (en) | 1994-06-15 | 1999-03-23 | Mobil Oil Corporation | Method and apparatus for breaking hydrocarbon emulsions |
US5705055A (en) * | 1995-06-23 | 1998-01-06 | Josam Company | Apparatus for automatically recovering grease from a grease separator |
US6055859A (en) | 1996-10-01 | 2000-05-02 | Agency Of Industrial Science And Technology | Non-contact micromanipulation method and apparatus |
US5951456A (en) | 1997-05-16 | 1999-09-14 | Scott; Harold W. | Ultrasonic methods and apparatus for separating materials in a fluid mixture |
CN2296230Y (en) | 1997-09-09 | 1998-11-04 | 耿连瑞 | Ultrasonic emulsion breaking device for raw oil electric field dehydration |
US6077400A (en) | 1997-09-23 | 2000-06-20 | Imperial Petroleum Recovery Corp. | Radio frequency microwave energy method to break oil and water emulsions |
KR100687967B1 (en) | 1999-11-16 | 2007-02-27 | 알엠지 서비시즈 피티와이 엘티디 | Treatment of crude oils |
US6770248B2 (en) | 2001-05-04 | 2004-08-03 | Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of National Defence Of Her Majesty's Canadian Government | Flowthrough device for the ultrasonic destruction of microorganisms in fluids |
CN2502767Y (en) | 2001-09-21 | 2002-07-31 | 王柱军 | Crude oil microwave dewatering treater |
CN2539559Y (en) | 2002-03-28 | 2003-03-12 | 中国石化集团齐鲁石油化工公司 | Crude oil ultrasonic wave-electric field combined desalination device |
US6860979B2 (en) | 2002-08-07 | 2005-03-01 | National Tank Company | Dual frequency electrostatic coalescence |
CN1245231C (en) | 2003-08-27 | 2006-03-15 | 中国石油化工股份有限公司 | Method and device for breaking oil water emulsion using combined action of forward current and countercurrent flow ultrasonic wave |
CN2669953Y (en) | 2003-09-05 | 2005-01-12 | 中国石油化工股份有限公司 | Demulsifying devices for oil and water emulsified materials |
JP2005169186A (en) | 2003-12-08 | 2005-06-30 | Horiba Ltd | Emulsion vanishing method, measuring method, and soil specimen cleaning method |
CN2721201Y (en) | 2004-08-27 | 2005-08-31 | 重庆渝能滤油机制造有限公司 | Ultrasonic vacuum separator of vacuum oil filter |
CN1330580C (en) | 2005-01-07 | 2007-08-08 | 大连理工大学 | Microwave demulsifying and purifying method for emulsifying liquid waste water |
CN1298814C (en) | 2005-01-07 | 2007-02-07 | 陈列 | Method for breaking emulsion and dewatering for emulsified raw oil using mirowave and device for realizing said method |
CN1295007C (en) | 2005-01-07 | 2007-01-17 | 辽宁大学 | Demulsifying process for emulsified crude oil |
CN2765652Y (en) | 2005-01-07 | 2006-03-22 | 陈列 | Device for breaking emulsion and removing water from emulsified crude oil by microwave |
US20060237372A1 (en) | 2005-04-22 | 2006-10-26 | Ge Betz, Inc. | Separation of drilling mud emulsions |
CN100506941C (en) | 2005-09-07 | 2009-07-01 | 南京工业大学 | Dirty oil dewatering process for refinery and oil field |
BRPI0700642B1 (en) | 2007-03-07 | 2015-04-14 | Petroleo Brasileiro Sa | Method for treating water / oil emulsions with microwaves |
CN100545241C (en) | 2007-04-29 | 2009-09-30 | 中国石油化工股份有限公司 | A kind of crude oil pulsing electrical desalting technique |
WO2009067362A2 (en) | 2007-11-21 | 2009-05-28 | Baker Hughes Incorporated | Treatment fluids that increase in viscosity at or above a threshold temperature and methods of formulating and using such fluids |
CN101161789B (en) | 2007-11-27 | 2010-11-24 | 辽宁大学 | Sand-containing emulsification crude oil demulsification method |
CN101550353B (en) | 2008-04-01 | 2013-03-27 | 哈尔滨理工大学 | Combined type crude oil electric dewatering high-voltage power source and controlling device thereof |
CN201181904Y (en) | 2008-04-01 | 2009-01-14 | 哈尔滨理工大学 | Combined primary oil electric dehydration high voltage power supply and its control device |
CN101845105A (en) | 2010-05-18 | 2010-09-29 | 马云峰 | Synthetic method of inverse emulsion of polyacrylamide |
US9249650B2 (en) * | 2010-12-15 | 2016-02-02 | Wallace Bruce | Clean solar energy to enhance oil and gas location separator recovery |
CN102091439B (en) | 2010-12-27 | 2013-03-20 | 重庆工商大学 | Emulsified oil water hammer harmonic wave demulsification device |
CN104684624B (en) | 2012-07-30 | 2016-10-12 | 陶氏环球技术有限责任公司 | For separating the cationic ethylene base imidazole radicals copolymer of O/w emulsion |
FR3005426A1 (en) * | 2013-05-13 | 2014-11-14 | Fonds De L Espci Georges Charpak | DEVICE FOR FORCE DRAINAGE OF MULTIPHASIC FLUID |
-
2017
- 2017-05-22 US US15/601,491 patent/US20180334621A1/en not_active Abandoned
-
2018
- 2018-05-22 WO PCT/US2018/033850 patent/WO2018217719A1/en active Application Filing
- 2018-05-22 EP EP18733718.3A patent/EP3630327A1/en not_active Withdrawn
- 2018-05-22 CN CN201880034055.0A patent/CN110678243B/en active Active
-
2021
- 2021-03-22 US US17/208,668 patent/US11873454B2/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1405119A (en) * | 1918-02-06 | 1922-01-31 | Petroleum Rectifying Co | Apparatus for dehydrating petroleum emulsions |
US2547190A (en) * | 1946-01-23 | 1951-04-03 | Maloney Crawford Tank And Mfg | Oil and gas separator |
US3098827A (en) * | 1958-03-31 | 1963-07-23 | Nalco Chemical Co | Demulsification of petroleum oil emulsions |
US20020015585A1 (en) * | 2000-06-09 | 2002-02-07 | Emerson Electric Company | Multivariable compact electric heater |
US20090107558A1 (en) * | 2007-10-23 | 2009-04-30 | Quigley Peter A | Heated pipe and methods of transporting viscous fluid |
WO2010134822A1 (en) * | 2009-05-22 | 2010-11-25 | Aker Process Systems As | Method and apparatus for breaking a stable emulsion |
US20170254564A1 (en) * | 2016-03-02 | 2017-09-07 | Watlow Electric Manufacturing Company | Heater bundle for adaptive control |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113620486A (en) * | 2021-08-23 | 2021-11-09 | 塔里木大学 | Organic chemistry experiment sewage treatment plant |
CN115445248A (en) * | 2022-09-16 | 2022-12-09 | 江苏理工学院 | Efficient sump oil treatment device integrating multiple demulsification technologies and treatment method thereof |
Also Published As
Publication number | Publication date |
---|---|
US11873454B2 (en) | 2024-01-16 |
EP3630327A1 (en) | 2020-04-08 |
US20210207040A1 (en) | 2021-07-08 |
CN110678243B (en) | 2022-08-23 |
CN110678243A (en) | 2020-01-10 |
WO2018217719A1 (en) | 2018-11-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11873454B2 (en) | Crude hydrocarbon fluids demulsification system | |
US11542444B2 (en) | Desalting plant systems and methods for enhanced tight emulsion crude oil treatment | |
RU2673054C2 (en) | Apparatus and method for gas and liquid separation | |
AU2006255609B2 (en) | Pipes, systems, and methods for transporting fluids | |
US20090065431A1 (en) | In-line separator | |
US9764252B2 (en) | System and method to treat a multiphase stream | |
US6533929B2 (en) | Heated inclined separation pressure vessel | |
US3025928A (en) | Oil and gas separator | |
WO2015036041A1 (en) | Hydrocarbon separation apparatus with recirculation loop | |
US4289204A (en) | Solar heat treating of well fluids | |
Ditria et al. | The separation of solids and liquids with hydrocyclone-based technology for water treatment and crude processing | |
US11517863B2 (en) | Water separation in flowlines or trunk lines | |
US10913903B2 (en) | System and method for using a flash evaporator to separate bitumen and hydrocarbon condensate | |
US4481109A (en) | Solar heat treating of well fluids | |
US11745121B2 (en) | Inline demulsification device | |
RU2209961C1 (en) | Method of well production separation and device for method embodiment | |
US10596489B2 (en) | Immersed plate heater separation system | |
AU2018252927B2 (en) | Inflow device | |
Dubay et al. | Utilization of Heat and Centrifuge Technology to Recover Crude for Sales from Slop Oil | |
WO2017190759A1 (en) | Injection-mixing device, fluid treatment system and method for mixing a first fluid and a second fluid | |
US3303232A (en) | Process for separating condensed hydrocarbons from natural gas and reducing pressure on the gas | |
Famisa | SPECIALIZATION PROJECT 2015 | |
WO2017018887A1 (en) | Transporting fluid from a well to a processing facility |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: SAUDI ARABIAN OIL COMPANY, SAUDI ARABIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:AMMINUDIN, KAMARUL ARIFFIN;MEERANPILLAI, NAGOORPITCHAI S.;OWAIDHI, SULTAN H.;SIGNING DATES FROM 20170516 TO 20170520;REEL/FRAME:042981/0240 |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: FINAL REJECTION MAILED |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
STPP | Information on status: patent application and granting procedure in general |
Free format text: ADVISORY ACTION MAILED |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |