US20190293280A1 - Plasma fired steam generator system - Google Patents

Plasma fired steam generator system Download PDF

Info

Publication number
US20190293280A1
US20190293280A1 US16/259,508 US201916259508A US2019293280A1 US 20190293280 A1 US20190293280 A1 US 20190293280A1 US 201916259508 A US201916259508 A US 201916259508A US 2019293280 A1 US2019293280 A1 US 2019293280A1
Authority
US
United States
Prior art keywords
steam
electrodes
plasma
high pressure
water
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
Application number
US16/259,508
Inventor
Lakshminarayana RAO
Pierre Carabin
Jean-Rene GAGNON
William Kreklewetz
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Pyrogenesis Canada Inc
Original Assignee
Pyrogenesis Canada Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Pyrogenesis Canada Inc filed Critical Pyrogenesis Canada Inc
Priority to US16/259,508 priority Critical patent/US20190293280A1/en
Assigned to PYROGENESIS CANADA INC. reassignment PYROGENESIS CANADA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CARABIN, PIERRE, GAGNON, JEAN-RENE, RAO, LAKSHMINARAYANA
Assigned to PYROGENESIS CANADA INC. reassignment PYROGENESIS CANADA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KREKLEWETZ, William
Publication of US20190293280A1 publication Critical patent/US20190293280A1/en
Priority to US17/942,772 priority patent/US20230250952A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/28Methods of steam generation characterised by form of heating method in boilers heated electrically
    • F22B1/30Electrode boilers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/48Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/48Devices for removing water, salt, or sludge from boilers; Arrangements of cleaning apparatus in boilers; Combinations thereof with boilers
    • F22B37/54De-sludging or blow-down devices

Definitions

  • the subject matter of the present disclosure relates to steam generation.
  • Bitumen contained in ore bodies is recovered using either surface mining with subsequent physical/mechanical recovery unit operations or with an in situ recovery process referred to as Steam assisted gravity drainage (SAGD).
  • SAGD Steam assisted gravity drainage
  • steam generated at a centralized boiler house using once through steam generators (OTSG) is transported to oil wells located at distances anywhere between 2 and 10 km.
  • the steam pressure at the OTSG is 10 MPa, while at the inlet of the well it is 4 MPa and inside the well it is 2.5 MPa.
  • the water-oil emulsion recovered from the oil well is then pumped to the central processing facility. Oil and water are separated from this emulsion using knock-out drums. Since environmental regulations require a high recycle ratio of water, the dirty water is re-used using a series of water cleaning unit operations before it can be used as boiler feed water for the OTSGs.
  • the existing water recovery/steam generation process has drawbacks and limitations that include, but are not limited to, high capital costs, long installation and commissioning times, long start-up and shutdown times and low process availability.
  • the current process is also not economically viable for smaller or isolated well pads.
  • the embodiments described herein provide in one aspect a steam generating system, which uses a combination of submerged plasma arcs and resistive heating, to generate high pressure steam from dirty feed water.
  • the embodiments described herein provide in another aspect a plasma fired steam generator, which uses either a single set of electrodes or multiple sets of electrodes to generate high pressure steam from the feed water.
  • inventions described herein provide in another aspect an electrode seal system which can provide the seal between the electrically conducting electrodes and the body of the plasma fired steam generator.
  • the embodiments described herein provide in another aspect an endless screw mechanism, which can provide great precision, used to control the relative position of the electrically conducting electrodes and thus independently control the current for each AC phase and the power input to a plasma fired steam generator (PFSG).
  • PFSG plasma fired steam generator
  • a plasma fired steam generator comprising either a single set of electrodes or multiple sets of electrodes to generate high pressure steam from feed water.
  • inventions described herein provide in another aspect an electrode seal system for use between electrically conducting electrodes and a body of a plasma fired steam generator.
  • the embodiments described herein provide in another aspect an endless screw mechanism for use in controlling a relative position of electrically conducting electrodes and thus independently controlling a current for each AC phase and a power input to a plasma fired steam generator.
  • a steam generating system comprising a combination of at least one submerged plasma arc and resistive heating, adapted to generate high pressure steam from dirty feed water.
  • the embodiments described herein provide in another aspect a method for generating steam, comprising: providing a steam generator; feeding dirty water to the steam generator; and submitting the dirty water to at least one submerged plasma arc and to resistive heating, such as to generate high pressure steam.
  • FIG. 1 shows a schematic representation of a plasma fired steam generator (PFSG) system according to one of various exemplary embodiments
  • FIGS. 2 a and 2 b show schematic representations of the PFSG with a single set of electrodes and with multiple sets of electrodes, respectively;
  • FIG. 3 shows a schematic representation of electrode seals, which are used to seal a gap between a current carrying electrode and a body of the PFSG;
  • FIG. 4 shows a schematic representation of an electrode motion system.
  • the present system uses a combination of plasma arcs and resistive heating, generated either using alternating current or direct current and submerged under water, to produce steam from untreated (dirty) water.
  • the energy needed to produce steam is provided by the plasma arcs struck between electrically conducting electrodes, as well as the water's electrical resistivity.
  • a high current, low voltage power source either AC or DC, is used to generate and power the plasma arcs.
  • the dirty water coming, for example, from the free water knock outs (FWKO) is directly injected into a plasma fired steam generator.
  • the plasma arcs submerged in the water, along with resistive heating, deliver the necessary energy to evaporate water and produce high pressure steam in a continuous manner.
  • the PFSG functions in a similar way to an electric arc furnace processing scrap steel, but using steel electrodes instead of graphite electrodes, and immersed in water, instead of in a mass of steel scrap.
  • the intense heat of the plasma will vaporize water at a high rate.
  • the main advantage of using plasma over gas or electric heating elements is that the intense heat of the plasma allows the electrodes tips to remain clean, despite the precipitation of solids caused by the evaporation of dirty water. This allows for a high throughput of steam production with a small installation footprint.
  • the Plasma Fired Steam Generator can be used to produce high pressure (4 MPa) steam from “dirty” water directly at the well pad. This eliminates the costly and sometimes dangerous transportation of high pressure steam over long distances, allows for quick expansion and allows for the use of brackish water as a make-up water source when required.
  • the PFSG can be built in modular sections, allowing for installation at a single well, or for an entire well pad, as required.
  • the dirty water used to produce steam is fed, via a feed inlet 8 , to a plasma fired steam generator (PFSG) 1 , powered by submerged electrodes 2 .
  • the water portion of the feed is evaporated to form steam, whereas the solid portion settles at the bottom of the steam generator 1 .
  • the steam generated is removed via a steam outlet 10 from the steam space, and the residual sludge is removed as a blowdown stream via a residue outlet 12 .
  • the plasma arcs are used to intermittently remove any scaling or solid deposits that can accumulate on the electrodes.
  • a vessel of the PFSG 1 is generally denoted by reference 14 .
  • FIGS. 2 a and 2 b show the electrode arrangement for the PFSG 1 with a single set of electrodes and multiple sets of electrodes, respectively.
  • PFSGs 1 equipped with multiple sets of electrodes are used, whereas smaller throughput steam generators 1 use only a single set of electrodes.
  • the PFSG includes a vertical steel cylindrical vessel 14 a with spherical ends designed to meet the appropriate requirements for steam pressure vessels.
  • the three alternating current (AC) electrodes are located, for instance, midway up the reactor's sidewall and are positioned at 120 degrees from each other.
  • a steam outlet 10 a is located, for instance, at the top of the reactor.
  • the reactor includes a horizontal steel cylinder 14 b with spherical ends, which meets the appropriate requirements for steam pressure vessels.
  • the AC electrodes are Installed, for example, as 6 trios (the electrodes of each trio being positioned at 120 degrees from one another about the reactor's circumference), for a total of 18 electrodes.
  • a steam outlet 10 b is located, for instance, in the middle of the reactor, with three sets of electrodes on each side. For larger capacity PFSGs 1 , additional sets of electrodes would be provided. For smaller capacity PFSGs 1 , between 2 and 6 sets of electrodes would be used.
  • An electrically insulating, high pressure seal mechanism is used to seal a gap between the current carrying electrodes 2 and a body of the PFSG 1 , as shown in FIG. 3 .
  • electrically insulating plates 3 and sleeves 4 are used.
  • the power input to the PFSG 1 is controlled by varying the power supply voltage set-point and also by varying the relative position of the electrodes with each other. Varying the position of the electrodes relative to each other allows for controlling the current, and consequently the total power input.
  • the power input to the PFSG 1 is controlled by varying the power supply current set-point and also by varying the relative position of the electrodes with each other. Varying the position of the electrodes relative to each other allows for controlling the voltage, and consequently the total power input.
  • Electrode damps 6 are fabricated from electrically conductive materials and, as they clamp onto the electrodes, they provide the necessary contact for the flow of electric current.
  • PFSG Plasma Fired Steam Generator

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Plasma Technology (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Discharge Heating (AREA)
  • Treatment Of Sludge (AREA)

Abstract

A system for generating high pressure steam from dirty water uses a combination of submerged plasma arcs and electrical resistive heating. Dirty water from steam assisted gravity drainage, or other dirty water producing process, which needs to be converted into high pressure steam, is fed directly without any pre-treatment, into a plasma fired steam generator, powered by submerged electrodes. The combination of electric arc plasma and resistive heating is created between the submerged electrodes. The heat so generated will boil the water portion of the dirty water feed to generate steam that is collected in a steam space and then removed therefrom. The solids and other residues (residual sludge) present in the feed water settle down at the bottom of the steam generator and are removed via a blow-down stream. The plasma arcs are used to intermittently remove any scaling or solid deposits that can accumulate on the electrodes.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • This Application claims priority on U.S. Provisional Application No. 61/877,150, now pending, filed on Sep. 12, 2013, which is herein incorporated by reference.
  • FIELD
  • The subject matter of the present disclosure relates to steam generation.
  • BACKGROUND
  • Bitumen contained in ore bodies (oil sands) is recovered using either surface mining with subsequent physical/mechanical recovery unit operations or with an in situ recovery process referred to as Steam assisted gravity drainage (SAGD). About 80-85% of the total oil sands reserves employ the SAGD process. In the SAGD process, steam generated at a centralized boiler house using once through steam generators (OTSG) is transported to oil wells located at distances anywhere between 2 and 10 km. The steam pressure at the OTSG is 10 MPa, while at the inlet of the well it is 4 MPa and inside the well it is 2.5 MPa. The water-oil emulsion recovered from the oil well is then pumped to the central processing facility. Oil and water are separated from this emulsion using knock-out drums. Since environmental regulations require a high recycle ratio of water, the dirty water is re-used using a series of water cleaning unit operations before it can be used as boiler feed water for the OTSGs.
  • The existing water recovery/steam generation process has drawbacks and limitations that include, but are not limited to, high capital costs, long installation and commissioning times, long start-up and shutdown times and low process availability. The current process is also not economically viable for smaller or isolated well pads.
  • SUMMARY
  • It would thus be highly desirable to be provided with a system or method that would at least partially address the disadvantages of the existing technologies.
  • The embodiments described herein provide in one aspect a steam generating system, which uses a combination of submerged plasma arcs and resistive heating, to generate high pressure steam from dirty feed water.
  • The embodiments described herein provide in another aspect a plasma fired steam generator, which uses either a single set of electrodes or multiple sets of electrodes to generate high pressure steam from the feed water.
  • The embodiments described herein provide in another aspect an electrode seal system which can provide the seal between the electrically conducting electrodes and the body of the plasma fired steam generator.
  • The embodiments described herein provide in another aspect an endless screw mechanism, which can provide great precision, used to control the relative position of the electrically conducting electrodes and thus independently control the current for each AC phase and the power input to a plasma fired steam generator (PFSG).
  • The embodiments described herein provide in another aspect a plasma fired steam generator, comprising either a single set of electrodes or multiple sets of electrodes to generate high pressure steam from feed water.
  • The embodiments described herein provide in another aspect an electrode seal system for use between electrically conducting electrodes and a body of a plasma fired steam generator.
  • The embodiments described herein provide in another aspect an endless screw mechanism for use in controlling a relative position of electrically conducting electrodes and thus independently controlling a current for each AC phase and a power input to a plasma fired steam generator.
  • The embodiments described herein provide in another aspect a steam generating system, comprising a combination of at least one submerged plasma arc and resistive heating, adapted to generate high pressure steam from dirty feed water.
  • The embodiments described herein provide in another aspect a method for generating steam, comprising: providing a steam generator; feeding dirty water to the steam generator; and submitting the dirty water to at least one submerged plasma arc and to resistive heating, such as to generate high pressure steam.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • For a better understanding of the embodiments described herein and to show more clearly how they may be carried into effect, reference will now be made, by way of example only, to the accompanying drawings which show at least one exemplary embodiment, and in which:
  • FIG. 1 shows a schematic representation of a plasma fired steam generator (PFSG) system according to one of various exemplary embodiments;
  • FIGS. 2a and 2b show schematic representations of the PFSG with a single set of electrodes and with multiple sets of electrodes, respectively;
  • FIG. 3 shows a schematic representation of electrode seals, which are used to seal a gap between a current carrying electrode and a body of the PFSG; and
  • FIG. 4 shows a schematic representation of an electrode motion system.
  • DESCRIPTION OF VARIOUS EMBODIMENTS
  • The present system uses a combination of plasma arcs and resistive heating, generated either using alternating current or direct current and submerged under water, to produce steam from untreated (dirty) water. The energy needed to produce steam is provided by the plasma arcs struck between electrically conducting electrodes, as well as the water's electrical resistivity. A high current, low voltage power source, either AC or DC, is used to generate and power the plasma arcs.
  • In the present system, called the plasma fired steam generator (PFSG) process, the dirty water coming, for example, from the free water knock outs (FWKO) is directly injected into a plasma fired steam generator. The plasma arcs submerged in the water, along with resistive heating, deliver the necessary energy to evaporate water and produce high pressure steam in a continuous manner.
  • The PFSG functions in a similar way to an electric arc furnace processing scrap steel, but using steel electrodes instead of graphite electrodes, and immersed in water, instead of in a mass of steel scrap. The intense heat of the plasma will vaporize water at a high rate. The main advantage of using plasma over gas or electric heating elements is that the intense heat of the plasma allows the electrodes tips to remain clean, despite the precipitation of solids caused by the evaporation of dirty water. This allows for a high throughput of steam production with a small installation footprint.
  • For the SAGD applications, the Plasma Fired Steam Generator (PFSG) can be used to produce high pressure (4 MPa) steam from “dirty” water directly at the well pad. This eliminates the costly and sometimes dangerous transportation of high pressure steam over long distances, allows for quick expansion and allows for the use of brackish water as a make-up water source when required.
  • Furthermore, the PFSG can be built in modular sections, allowing for installation at a single well, or for an entire well pad, as required.
  • As shown in FIG. 1, the dirty water used to produce steam is fed, via a feed inlet 8, to a plasma fired steam generator (PFSG) 1, powered by submerged electrodes 2. The water portion of the feed is evaporated to form steam, whereas the solid portion settles at the bottom of the steam generator 1. The steam generated is removed via a steam outlet 10 from the steam space, and the residual sludge is removed as a blowdown stream via a residue outlet 12. The plasma arcs are used to intermittently remove any scaling or solid deposits that can accumulate on the electrodes. A vessel of the PFSG 1 is generally denoted by reference 14.
  • Therefore, dirty water from the Steam Assisted Gravity Drainage (SAGD), or other dirty water producing process, which needs to be converted into high pressure steam, is fed typically directly without any pretreatment into the plasma fired steam generator (PFSG) 1. A combination of electric arc plasma and resistive heating is created between the submerged electrodes 2. The heat so generated will boil the water to generate steam which is collected in the steam space. The solids and other residues present in the feed water settle down at the bottom of the (PFSG) 1, and are removed via a blowdown stream.
  • FIGS. 2a and 2b show the electrode arrangement for the PFSG 1 with a single set of electrodes and multiple sets of electrodes, respectively. To achieve higher steam throughput, PFSGs 1 equipped with multiple sets of electrodes are used, whereas smaller throughput steam generators 1 use only a single set of electrodes.
  • In the 3 phase AC arrangement with a single set of electrodes illustrated in FIG. 2a , the PFSG includes a vertical steel cylindrical vessel 14 a with spherical ends designed to meet the appropriate requirements for steam pressure vessels. The three alternating current (AC) electrodes are located, for instance, midway up the reactor's sidewall and are positioned at 120 degrees from each other. A steam outlet 10 a is located, for instance, at the top of the reactor.
  • In the multiple set of electrodes 3 phase AC arrangement of FIG. 2b , the reactor includes a horizontal steel cylinder 14 b with spherical ends, which meets the appropriate requirements for steam pressure vessels. The AC electrodes are Installed, for example, as 6 trios (the electrodes of each trio being positioned at 120 degrees from one another about the reactor's circumference), for a total of 18 electrodes. A steam outlet 10 b is located, for instance, in the middle of the reactor, with three sets of electrodes on each side. For larger capacity PFSGs 1, additional sets of electrodes would be provided. For smaller capacity PFSGs 1, between 2 and 6 sets of electrodes would be used.
  • An electrically insulating, high pressure seal mechanism is used to seal a gap between the current carrying electrodes 2 and a body of the PFSG 1, as shown in FIG. 3. To maintain electrical insulation and thus avoid a flow of electric current through the body of the PFSG 1, electrically insulating plates 3 and sleeves 4 are used.
  • In the AC mode of operation, the power input to the PFSG 1 is controlled by varying the power supply voltage set-point and also by varying the relative position of the electrodes with each other. Varying the position of the electrodes relative to each other allows for controlling the current, and consequently the total power input.
  • In the DC mode of operation, the power input to the PFSG 1 is controlled by varying the power supply current set-point and also by varying the relative position of the electrodes with each other. Varying the position of the electrodes relative to each other allows for controlling the voltage, and consequently the total power input.
  • The electrodes of the PFSG 1 are moved using an electrode motion system, for example an endless screw mechanism 5, as shown in FIG. 4, which can be controlled with great precision and can maintain the electrode positions against the force of the high pressure steam. Electrode damps 6 are fabricated from electrically conductive materials and, as they clamp onto the electrodes, they provide the necessary contact for the flow of electric current.
  • Although the application mentioned hereinabove of the present Plasma Fired Steam Generator (PFSG) 1 is for the extraction of bitumen from the oil sands, it is however noted that the PFSG can be used in any Industrial processes where a source of dirty water must be purified before conversion to steam at low or high pressure.
  • Finally, while the above description provides examples of the embodiments, it will be appreciated that some features and/or functions of the described embodiments are susceptible to modification without departing from the spirit and principles of operation of the described embodiments. Accordingly, what has been described above has been Intended to be illustrative of the embodiments and non-limiting, and it will be understood by persons skilled in the art that other variants and modifications may be made without departing from the scope of the embodiments as defined in the claims appended hereto.

Claims (22)

1.-7. (canceled)
8. An endless screw mechanism for use in controlling a relative position of electrically conducting electrodes and thus independently controlling a current for each AC phase and a power Input to a plasma fired steam generator.
9. A steam generating system, comprising a combination of at least one submerged plasma are and resistive heating, adapted to generate high pressure steam from dirty feed water.
10. The steam generating system of claim 9, comprising a vessel, at least one inlet to the vessel for feeding the dirty feed water therein, and at least one first outlet for removing the high pressure steam from the vessel.
11. The steam generating system of claim 9, comprising at least one second outlet for removing solids and other residues from the vessel.
12. The steam generating system of claim 9, wherein there are provided a plurality of submerged plasma arcs.
13. The steam generating system of claim 9, comprising either a single set of electrodes or multiple sets of electrodes to generate the high pressure steam from the dirty feed water.
14. The steam generating system of claim 9, wherein there is provided an electrode seal system between electrically conducting electrodes and a body of the vessel.
15. The steam generating system of claim 14, wherein electrically insulating plate(s) and sleeve(s) are provided to maintain electrical Insulation and thus avoid a flow of electric current through the body of the vessel.
16. (canceled)
17. The steam generating system of claim 9, wherein the steam generating system Includes a plasma fired steam generator.
18. A method for generating steam, comprising:
providing a steam generator;
feeding dirty water to the steam generator; and
submitting the dirty water to at least one submerged plasma arc and to resistive heating, such as to generate high pressure steam.
19. The method of claim 18, further comprising the step of removing the high pressure steam from the steam generator.
20. The method of claim 18, further comprising the step of removing a residual sludge from the steam generator.
21. The method of claim 18, wherein the dirty water is obtained from steam assisted gravity drainage, or another dirty water producing process.
22. The method of claim 18, wherein the dirty water is fed directly without any pre-treatment into the steam generator.
23. The method of claim 18, wherein there are provided a plurality of submerged electrodes.
24. The method of claim 18, wherein a combination of electric arc plasma and resistive heating is created between submerged electrodes.
25. The method of claim 18, wherein the heat generated is adapted to boll a water portion of the dirty water to generate the high pressure steam.
26. The method of claim 18, wherein the high pressure steam is collected in a steam space and is then removed therefrom.
27. The method of claim 18, wherein solids and other residues (residual sludge) present in the dirty water settle down at a bottom of the steam generator and are removed via a blow-down stream.
28. The method of claim 18, wherein the plasma arcs are used to intermittently remove scaling or solid deposits that may have accumulated on the electrodes.
US16/259,508 2013-09-12 2019-01-28 Plasma fired steam generator system Abandoned US20190293280A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US16/259,508 US20190293280A1 (en) 2013-09-12 2019-01-28 Plasma fired steam generator system
US17/942,772 US20230250952A1 (en) 2013-09-12 2022-09-12 Plasma fired steam generator system

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201361877150P 2013-09-12 2013-09-12
PCT/CA2014/000679 WO2015035502A1 (en) 2013-09-12 2014-09-12 Plasma fired steam generator system
US201615021899A 2016-03-14 2016-03-14
US16/259,508 US20190293280A1 (en) 2013-09-12 2019-01-28 Plasma fired steam generator system

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
US15/021,899 Continuation US10253971B2 (en) 2013-09-12 2014-09-12 Plasma fired steam generator system
PCT/CA2014/000679 Continuation WO2015035502A1 (en) 2013-09-12 2014-09-12 Plasma fired steam generator system

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/942,772 Continuation US20230250952A1 (en) 2013-09-12 2022-09-12 Plasma fired steam generator system

Publications (1)

Publication Number Publication Date
US20190293280A1 true US20190293280A1 (en) 2019-09-26

Family

ID=52664872

Family Applications (3)

Application Number Title Priority Date Filing Date
US15/021,899 Active 2035-01-17 US10253971B2 (en) 2013-09-12 2014-09-12 Plasma fired steam generator system
US16/259,508 Abandoned US20190293280A1 (en) 2013-09-12 2019-01-28 Plasma fired steam generator system
US17/942,772 Abandoned US20230250952A1 (en) 2013-09-12 2022-09-12 Plasma fired steam generator system

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US15/021,899 Active 2035-01-17 US10253971B2 (en) 2013-09-12 2014-09-12 Plasma fired steam generator system

Family Applications After (1)

Application Number Title Priority Date Filing Date
US17/942,772 Abandoned US20230250952A1 (en) 2013-09-12 2022-09-12 Plasma fired steam generator system

Country Status (4)

Country Link
US (3) US10253971B2 (en)
CA (2) CA2924135C (en)
EA (1) EA201690589A1 (en)
WO (1) WO2015035502A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT202100001781A1 (en) * 2021-03-29 2022-09-29 Nigris Ferdinando De PLASMA-ELECTROLYTIC REACTOR SATURATED STEAM GENERATOR FED WITH SALT WATER AND 230VDC VOLTAGE

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144546A (en) * 1964-08-11 Immersed electrode heater for liquids
US2572337A (en) * 1946-09-13 1951-10-23 William B Harris Electric water heater
US2599806A (en) * 1949-09-29 1952-06-10 Norbert R Benchemoul Variable liquid resistance apparatus
US2757272A (en) * 1955-01-14 1956-07-31 Santoni Mariano Apparatus for the heating of liquids
US2847550A (en) * 1957-12-12 1958-08-12 Vilbiss Co Electric steam vaporizer
NL238400A (en) * 1958-04-21
US3081393A (en) * 1958-07-15 1963-03-12 Robert J Wohl Electric vaporizers
US3104308A (en) * 1960-02-15 1963-09-17 Ernest E Wilson Electrically operated continuous steam generator
US3389535A (en) * 1964-06-03 1968-06-25 Armetti Massimo Protective packaging of plastic material for vials and the like, as well as process and equipment for obtaining it
US3385950A (en) * 1965-10-04 1968-05-28 Edward R. Lipor Electrode type bottle warmer having time-controlled operation
US4772775A (en) 1987-03-23 1988-09-20 Leach Sam L Electric arc plasma steam generation
FR2669679B1 (en) * 1990-11-28 1994-04-29 Sud Ouest Conception Aeronauti GAS EJECTION NOZZLE FOR A REACTION ENGINE AND A REACTION ENGINE EQUIPPED WITH SUCH A NOZZLE, PARTICULARLY A SEPARATE FLOW TYPE ENGINE.
US6536523B1 (en) * 1997-01-14 2003-03-25 Aqua Pure Ventures Inc. Water treatment process for thermal heavy oil recovery
US20060042251A1 (en) 2004-08-30 2006-03-02 Villalobos Victor M Arc-electrolysis steam generator with energy recovery, and method therefor
US7327951B2 (en) * 2005-04-21 2008-02-05 Ivanhoe Chaput Instant water heater with PTC plastic conductive electrodes
RU2350836C2 (en) 2006-12-12 2009-03-27 Сергей Владимирович Гаврилов Method and device for obtaining water vapour from water
FR2918583B1 (en) * 2007-07-13 2011-06-10 Commissariat Energie Atomique PORTABLE GAS GENERATING DEVICE AND FUEL CELL POWER SUPPLY PROVIDED WITH SUCH A DEVICE
US8776522B2 (en) * 2008-04-15 2014-07-15 Morningside Venture Investments Limited Water reclamation system and method
CA2715619A1 (en) * 2009-11-12 2011-05-12 Maoz Betzer-Zilevitch Steam drive direct contact steam generation
US9114406B2 (en) * 2009-12-10 2015-08-25 Ex-Tar Technologies Steam driven direct contact steam generation
WO2011082301A2 (en) * 2009-12-30 2011-07-07 Vitag Holdings, Llc Bioorganically-augmented high value fertilizer
KR101310340B1 (en) * 2012-02-15 2013-09-23 한국수력원자력 주식회사 A steam generator reducing sludge and the method for manufacturing the tube sheet of a steam generator reducing sludge
US20140008208A1 (en) * 2012-07-05 2014-01-09 Garry Pichach Thermal system and process for producing steam from oilfield produced water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT202100001781A1 (en) * 2021-03-29 2022-09-29 Nigris Ferdinando De PLASMA-ELECTROLYTIC REACTOR SATURATED STEAM GENERATOR FED WITH SALT WATER AND 230VDC VOLTAGE

Also Published As

Publication number Publication date
US20160223188A1 (en) 2016-08-04
WO2015035502A1 (en) 2015-03-19
CA2924135A1 (en) 2015-03-19
US10253971B2 (en) 2019-04-09
CA3203760A1 (en) 2015-03-19
CA2924135C (en) 2023-08-22
EA201690589A1 (en) 2016-07-29
US20230250952A1 (en) 2023-08-10

Similar Documents

Publication Publication Date Title
CA2697810C (en) Method and apparatus for in situ extraction of bitumen or very heavy oil
US20230250952A1 (en) Plasma fired steam generator system
US8236150B2 (en) Plasma-arc-through apparatus and process for submerged electric arcs
US11686469B2 (en) Plasma assisted, dirty water, direct steam generation system, apparatus and method
US20090133643A1 (en) Method and apparatus for steam generation
US8739866B2 (en) Method for extracting bitumen and/or ultra-heavy oil from an underground deposit, associated installation and operating method for said installation
WO2012106631A1 (en) System and method for electrolyzing water
US20160097004A1 (en) Processes for desalting crude oil under dynamic flow conditions
US11186781B2 (en) Pulsed power supply
JP4444052B2 (en) Desalination equipment
KR101296267B1 (en) Recycling apparatus for waste wire
US20150308231A1 (en) Liquid based boiler
CA2904298A1 (en) Produced water steam generation process using produced water boiler with gas turbine
Drelich et al. The effect of electric field pulsation frequency on breaking water-in-oil emulsions
US20140166263A1 (en) Brine based indirect steam boiler
KR20150135158A (en) Apparatus for extracting and recovery metals from waste water
US20140166281A1 (en) Liquid indirect steam boiler
RU2422492C1 (en) Procedure for processing oil containing fractions and device for its implementation
US20230115790A1 (en) Direct contact process and method for producing hot water using mature fine tailings (mft) feedwater
CA2885081A1 (en) Steam generation system
KR20170080918A (en) Hydrate inhibitor treatment system
CA3133905A1 (en) Direct contact process and method for producing hot water using mature fine tailings (mft) feedwater
CA3017428C (en) Processes and systems for generating steam from produced water
RU2706316C1 (en) Magnetoelectric dehydrator
US20160076346A1 (en) Distributed steam generation process for use in hydrocarbon recovery operations

Legal Events

Date Code Title Description
AS Assignment

Owner name: PYROGENESIS CANADA INC., CANADA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:RAO, LAKSHMINARAYANA;CARABIN, PIERRE;GAGNON, JEAN-RENE;REEL/FRAME:048158/0520

Effective date: 20150608

AS Assignment

Owner name: PYROGENESIS CANADA INC., QUEBEC

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:KREKLEWETZ, WILLIAM;REEL/FRAME:048222/0241

Effective date: 20150608

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: FINAL REJECTION MAILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION