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US20170184305A1 - Gas saving device - Google Patents

Gas saving device Download PDF

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Publication number
US20170184305A1
US20170184305A1 US15/302,026 US201515302026A US2017184305A1 US 20170184305 A1 US20170184305 A1 US 20170184305A1 US 201515302026 A US201515302026 A US 201515302026A US 2017184305 A1 US2017184305 A1 US 2017184305A1
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US
United States
Prior art keywords
gas
fitting
steam trap
saving device
centrifugation
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
US15/302,026
Inventor
Alfredo GONZALEZ QUINTANA
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of US20170184305A1 publication Critical patent/US20170184305A1/en
Abandoned legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/02—Liquid fuel
    • F23K5/14—Details thereof
    • F23K5/18—Cleaning or purging devices, e.g. filters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46—Details
    • F23D14/68—Treating the combustion air or gas, e.g. by filtering, or moistening
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/002—Gaseous fuel
    • F23K5/007—Details
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C3/00—Stoves or ranges for gaseous fuels
    • F24C3/12—Arrangement or mounting of control or safety devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K2400/00—Pretreatment and supply of gaseous fuel
    • F23K2400/10—Pretreatment
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K2400/00—Pretreatment and supply of gaseous fuel
    • F23K2400/20—Supply line arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/02—Liquid fuel

Definitions

  • the object of the present invention is a device which, being placed downstream of the pressure regulator in a facility for the supply of liquefied petroleum gases or natural gas, improves fuel consumption efficiency in the facility, through loss recovery and impurities removal, by means of a filtering process, and stabilization of the gas flow by rearranging the molecules thereof.
  • Liquefied petroleum gases are a mixture of butane and propane, the main component of natural gas being methane which represents between 70% and 90% of the composition thereof. Both can be supplied for consumption in tanks either fixed or portable; in the case of fixed tanks the filling thereof is carried out by means of tankers, and in the case of portable tanks the filling thereof is carried out in industrial plants and its supply to the final user is carried out by replacing the empty tank for a full one.
  • the facility is similar both for natural gas and for liquefied petroleum gases, and it comprises a storage tank, a pressure regulator which reduces the fuel pressure inside the tank and controls the outgoing flow, the conveying pipeline which conveys the gas up to the devices consuming said fuel and among which there can be mentioned heating or household hot water boilers, cookers having gas burners or even fridges which use gas as an energy source.
  • the efficiency of these facilities depends on the flow rate and the supply pressure and on the impurities percentage the natural gas or liquefied petroleum gases contain.
  • the supply pressure and flow rate are reduced by the pressure drop produced by the facility pipes and connections, such as shut-off cocks.
  • the supplied gas has certain impurities, such as other hydrocarbons, sulphur, water and other type of substances which, in its combustion process, produce highly polluting emissions or reduce the efficiency thereof.
  • the invention disclosed solves the aforementioned drawbacks by means of a device which features easy mounting and maintenance, cheap manufacturing costs, which improves combustion efficiency and which reduces polluting emissions.
  • the gas saving device for liquefied petroleum gases or natural gas object of the present invention is of the type which are mounted downstream of the pressure regulator and upstream of the devices consuming the liquefied petroleum gases or the natural gas, such as, among others, boilers, cookers, fridges, etc . . .
  • the gas saving device comprises the following elements:
  • FIG. 1 Plan view of an outline of the saving gas device.
  • FIG. 1 shows a preferred embodiment of the gas saving device.
  • the gas saving device shown in FIG. 1 is connected downstream to the natural gas or liquefied petroleum gases inlet pipe.
  • the gas enters through a central inlet passage ( 2 ) into the first three-way T-fitting ( 1 ), and the flow thereof splits going out through the two side outlet passages ( 3 ) towards the side inlet passages ( 6 ) of the second three-way T-fitting ( 5 ), through the flexible or rigid pipes ( 4 ). Both flows coming from the first three-way T-fitting ( 1 ) are joined in the central outlet passage of the second fitting ( 7 ), increasing the gas pressure.
  • the gas flows into the steam trap ( 8 ) where the impurities contained therein are deposited; furthermore, the gas flows into said steam trap through an activated carbon filter ( 9 ), improving the particle and impurities capture, thus achieving the gas to come out substantially pure.
  • the gas flows through a copper centrifugation coil ( 10 ), wherein the gas molecules rearrangement is achieved, obtaining flow stabilization in the facility and improving the circulation thereof.
  • the gas flows towards the consuming devices, through the flow rate regulator ( 11 ) which regularizes the gas flow to the consumption requirements.
  • connections among the different elements of the invention and the supply facility are hermetically connected by means of the corresponding fittings and connections, such as gaskets, sealing elements, to guarantee the tightness of the facility and therefore to avoid gas leaks which can cause dangerous explosions.
  • the gas saving device disclosed in the present invention increases the gas pressure and supply flow rate so as to fulfil the requirements of the devices consuming said gas, eliminates the impurities it contains and prevents the problem of freezing by insufficient gas vaporization, thereby causing the combustion to produce a less amount of polluting emissions and particles, and making said combustion be more efficient.
  • Another one of the multiple advantages of the invention is that the mounting thereof does not require modifications in the general facility already installed, but only the connection thereof to the inlet pipe for the gas supply.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Centrifugal Separators (AREA)

Abstract

The present invention consists of a saving gas device which, being placed downstream of the pressure regulator and upstream of the consuming devices, in a natural gas or liquefied petroleum gases supply facility, improves the gas consumption efficiency by means of a recirculation, filtering and centrifugation process. The action exerted on the steam trap of the device, retains the impurities the gas contains, thus improving retention of particles and achieving the gas to come out substantially pure, as well as achieving gas molecules rearrangement by means of a centrifugation coil, obtaining flow stabilization and improving the circulation thereof.

Description

    OBJECT OF THE INVENTION
  • The object of the present invention is a device which, being placed downstream of the pressure regulator in a facility for the supply of liquefied petroleum gases or natural gas, improves fuel consumption efficiency in the facility, through loss recovery and impurities removal, by means of a filtering process, and stabilization of the gas flow by rearranging the molecules thereof.
    • BACKGROUND OF THE INVENTION
  • It is well known in the state of the art the use of liquefied petroleum gases that are present in natural gas, which is used as fuel in domestic, commercial and industrial environments.
  • Liquefied petroleum gases are a mixture of butane and propane, the main component of natural gas being methane which represents between 70% and 90% of the composition thereof. Both can be supplied for consumption in tanks either fixed or portable; in the case of fixed tanks the filling thereof is carried out by means of tankers, and in the case of portable tanks the filling thereof is carried out in industrial plants and its supply to the final user is carried out by replacing the empty tank for a full one.
  • The facility is similar both for natural gas and for liquefied petroleum gases, and it comprises a storage tank, a pressure regulator which reduces the fuel pressure inside the tank and controls the outgoing flow, the conveying pipeline which conveys the gas up to the devices consuming said fuel and among which there can be mentioned heating or household hot water boilers, cookers having gas burners or even fridges which use gas as an energy source.
  • The efficiency of these facilities depends on the flow rate and the supply pressure and on the impurities percentage the natural gas or liquefied petroleum gases contain. The supply pressure and flow rate are reduced by the pressure drop produced by the facility pipes and connections, such as shut-off cocks.
  • On the other hand, the supplied gas has certain impurities, such as other hydrocarbons, sulphur, water and other type of substances which, in its combustion process, produce highly polluting emissions or reduce the efficiency thereof.
  • The invention disclosed solves the aforementioned drawbacks by means of a device which features easy mounting and maintenance, cheap manufacturing costs, which improves combustion efficiency and which reduces polluting emissions.
    • DESCRIPTION OF THE INVENTION
  • The gas saving device for liquefied petroleum gases or natural gas object of the present invention, is of the type which are mounted downstream of the pressure regulator and upstream of the devices consuming the liquefied petroleum gases or the natural gas, such as, among others, boilers, cookers, fridges, etc . . .
  • The gas saving device comprises the following elements:
      • A first inlet three-way T-fitting, having a central passage as a gas inlet and two side passages as a gas outlet, wherein the inlet central passage is connected to the pipe coming from the pressure regulator;
      • A second outlet three-way T-fitting, having two side inlet passages and a central outlet passage, and wherein the central passage is connected to the first end of the steam trap;
      • Two flexible or rigid pipes which connect the side outlet passages of the first fitting to the side inlet passages of the second fitting.
      • A steam trap having a cylindrical shape and with the inner diameter thereof being longer than the inner diameter of the passages of the first and second fittings.
      • Inside the steam trap, the gas is first passed through an activated carbon filter, through which all the impurities carried in the gas are eliminated.
      • Next, the gas is passed through a copper coil which causes a centrifugation by means of which the rearrangement of the molecules thereof is achieved.
      • A flow rate regulator, wherein the end thereof situated downstream of said flow rate regulator is connected to the second end of the steam trap, and the end thereof situated upstream of the flow rate regulator is connected to the supply pipe of the consuming devices.
  • By means of the gas filtering, using activated carbon, practically all particle and impurities are removed, thus improving the effect of the steam chamber as far as filtering is concerned. Furthermore, by using the copper centrifugation coil the rearrangement of gas molecules is achieved, improving the stability of the flow rate throughout the whole facility and reducing the friction loss.
    • DESCRIPTION OF THE DRAWINGS
  • FIG. 1: Plan view of an outline of the saving gas device.
    •  LIST OF REFERENCES
  • 1.—First inlet three-way T-fitting
  • 2.—Central inlet passage of the first fitting
  • 3.—Side inlet passage of the first fitting
  • 4.—Flexible or rigid pipes
  • 5.—Second outlet three-way T-fitting
  • 6.—Side inlet passage of the second fitting
  • 7.—Central outlet passage of the second fitting.
  • 8.—Steam trap
  • 9.—Activated carbon filter
  • 10.—Copper centrifugation coil
  • 11.—Flow rate regulator
    • PREFERRED EMBODIMENT OF THE INVENTION
  • FIG. 1 shows a preferred embodiment of the gas saving device.
  • The gas saving device shown in FIG. 1 is connected downstream to the natural gas or liquefied petroleum gases inlet pipe. The gas enters through a central inlet passage (2) into the first three-way T-fitting (1), and the flow thereof splits going out through the two side outlet passages (3) towards the side inlet passages (6) of the second three-way T-fitting (5), through the flexible or rigid pipes (4). Both flows coming from the first three-way T-fitting (1) are joined in the central outlet passage of the second fitting (7), increasing the gas pressure. Then, the gas flows into the steam trap (8) where the impurities contained therein are deposited; furthermore, the gas flows into said steam trap through an activated carbon filter (9), improving the particle and impurities capture, thus achieving the gas to come out substantially pure. Still inside the steam trap (8), the gas flows through a copper centrifugation coil (10), wherein the gas molecules rearrangement is achieved, obtaining flow stabilization in the facility and improving the circulation thereof. And after said step, the gas flows towards the consuming devices, through the flow rate regulator (11) which regularizes the gas flow to the consumption requirements.
  • It is well known by those skilled in the art that the connections among the different elements of the invention and the supply facility are hermetically connected by means of the corresponding fittings and connections, such as gaskets, sealing elements, to guarantee the tightness of the facility and therefore to avoid gas leaks which can cause dangerous explosions.
  • The gas saving device disclosed in the present invention, increases the gas pressure and supply flow rate so as to fulfil the requirements of the devices consuming said gas, eliminates the impurities it contains and prevents the problem of freezing by insufficient gas vaporization, thereby causing the combustion to produce a less amount of polluting emissions and particles, and making said combustion be more efficient.
  • Another one of the multiple advantages of the invention is that the mounting thereof does not require modifications in the general facility already installed, but only the connection thereof to the inlet pipe for the gas supply.

Claims (2)

1. Gas saving device.—of the type being mounted downstream of the pressure regulator and upstream of the consuming devices characterized in that it features a steam trap (8) having a cylindrical shape containing inside first an activated carbon filter (9) and then a copper centrifugation coil (10), and a flow rate regulator (11) connected to the supply pipe for the consuming devices.
2. Gas saving device.—according to claim 1, characterized in that it comprises a steam trap (8) the diameter of which is longer than the inner diameter of the passages of the first and second fitting.
US15/302,026 2014-04-08 2015-03-12 Gas saving device Abandoned US20170184305A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
ESP201430523 2014-04-08
ES201430523A ES2547957B1 (en) 2014-04-08 2014-04-08 Gas saving device
PCT/ES2015/070175 WO2015155388A1 (en) 2014-04-08 2015-03-12 Gas-saving device

Publications (1)

Publication Number Publication Date
US20170184305A1 true US20170184305A1 (en) 2017-06-29

Family

ID=54250611

Family Applications (1)

Application Number Title Priority Date Filing Date
US15/302,026 Abandoned US20170184305A1 (en) 2014-04-08 2015-03-12 Gas saving device

Country Status (6)

Country Link
US (1) US20170184305A1 (en)
EP (1) EP3147572B1 (en)
ES (2) ES2547957B1 (en)
MX (1) MX362395B (en)
PT (1) PT3147572T (en)
WO (1) WO2015155388A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2535994B (en) * 2015-02-27 2018-08-01 Eco Device Ltd Gas saving device

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US3347026A (en) * 1965-01-14 1967-10-17 Mc Graw Edison Co Fluid separator
US3394533A (en) * 1966-06-17 1968-07-30 Lockheed Aircraft Corp Liquid-gas separator
US3977850A (en) * 1976-02-17 1976-08-31 Combustion Engineering, Inc. Centrifugal separator
US4284504A (en) * 1979-10-09 1981-08-18 Hastings Manufacturing Company Centrifugal spin-on filter or separator and method of making and assembling the same
US4297116A (en) * 1978-07-10 1981-10-27 Aitken, Inc. Apparatus for separating foreign matter from a gas stream
US4938787A (en) * 1986-10-31 1990-07-03 Simmerlein Erlbacher E W Filter device and filter apparatus comprising such filter devices
US5271232A (en) * 1990-07-20 1993-12-21 Toshiba Ceramics Co., Ltd. Filtration apparatus
US5364540A (en) * 1993-02-11 1994-11-15 Emerson Electric Co. Filter drier and method of filtering a fluid stream
US5440919A (en) * 1994-08-29 1995-08-15 Spectronics Corporation Method of introducing leak detection dye into an air conditioning or refrigeration system
US5665902A (en) * 1994-05-10 1997-09-09 American Air Liquide, Inc. Method to analyze particle contaminants in compressed gases
US5775442A (en) * 1996-10-25 1998-07-07 Northland Production Testing, Ltd. Recovery of gas from drilling fluid returns in underbalanced drilling
US6044649A (en) * 1997-12-22 2000-04-04 Matsushita Electric Industrial Co., Ltd. Air conditioner
US6083291A (en) * 1996-09-05 2000-07-04 Jgc Corporation Gas transfer pipe arrangement
US6302932B1 (en) * 1998-11-12 2001-10-16 Honeywell International, Inc. Combined water coalescer odor removal filter for use in water separation systems
US20030102051A1 (en) * 2001-11-30 2003-06-05 Satoshi Hasaka Container valve
US20030140792A1 (en) * 2002-01-25 2003-07-31 Sporlan Valve Company Molded core filter drier with filter media molded to core for use in heat pump systems
US20030140793A1 (en) * 2002-01-25 2003-07-31 Sporlan Valve Company Molded core filter drier with filter media molded to core
US7132011B2 (en) * 2003-09-02 2006-11-07 Entegris, Inc. Reactive gas filter
US7278401B1 (en) * 2004-10-29 2007-10-09 Walbro Engine Management, L.L.C. Fuel pressure regulator housing
US20080005919A1 (en) * 2006-07-10 2008-01-10 Brown Jerome R In-line dryer
US20090288427A1 (en) * 2008-05-21 2009-11-26 Raytheon Company Isothermal gas supply and method for minimizing the temperature excursion of a gas mixture released therefrom
US20150083425A1 (en) * 2012-05-08 2015-03-26 Release Energy Pty Ltd Inline non-targeted component removal
US20150298040A1 (en) * 2012-12-14 2015-10-22 Entegris, Inc. Gas Purification Filter Unit

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CN201715535U (en) * 2010-05-28 2011-01-19 山西阳煤丰喜肥业(集团)有限责任公司 Device for simply removing dust before blowing air entering into combustion furnace
ES1079980Y (en) * 2013-05-03 2013-08-26 Quintana Alfredo Gonzalez ALTERNATE RECOVERY DEVICE FOR INSTALLATIONS OF LIQUID GASES OF PETROLEUM OR NATURAL GAS
ES1142356Y (en) * 2014-12-18 2015-11-10 Plaza Francisco Valdesoiro Filter for gas saving and environmental purification

Patent Citations (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3186150A (en) * 1962-10-01 1965-06-01 Mc Graw Edison Co Apparatus for the treatment of gases
US3347026A (en) * 1965-01-14 1967-10-17 Mc Graw Edison Co Fluid separator
US3394533A (en) * 1966-06-17 1968-07-30 Lockheed Aircraft Corp Liquid-gas separator
US3977850A (en) * 1976-02-17 1976-08-31 Combustion Engineering, Inc. Centrifugal separator
US4297116A (en) * 1978-07-10 1981-10-27 Aitken, Inc. Apparatus for separating foreign matter from a gas stream
US4284504A (en) * 1979-10-09 1981-08-18 Hastings Manufacturing Company Centrifugal spin-on filter or separator and method of making and assembling the same
US4938787A (en) * 1986-10-31 1990-07-03 Simmerlein Erlbacher E W Filter device and filter apparatus comprising such filter devices
US5271232A (en) * 1990-07-20 1993-12-21 Toshiba Ceramics Co., Ltd. Filtration apparatus
US5364540A (en) * 1993-02-11 1994-11-15 Emerson Electric Co. Filter drier and method of filtering a fluid stream
US5665902A (en) * 1994-05-10 1997-09-09 American Air Liquide, Inc. Method to analyze particle contaminants in compressed gases
US5440919A (en) * 1994-08-29 1995-08-15 Spectronics Corporation Method of introducing leak detection dye into an air conditioning or refrigeration system
US6083291A (en) * 1996-09-05 2000-07-04 Jgc Corporation Gas transfer pipe arrangement
US5775442A (en) * 1996-10-25 1998-07-07 Northland Production Testing, Ltd. Recovery of gas from drilling fluid returns in underbalanced drilling
US6044649A (en) * 1997-12-22 2000-04-04 Matsushita Electric Industrial Co., Ltd. Air conditioner
US6302932B1 (en) * 1998-11-12 2001-10-16 Honeywell International, Inc. Combined water coalescer odor removal filter for use in water separation systems
US20030102051A1 (en) * 2001-11-30 2003-06-05 Satoshi Hasaka Container valve
US20030140792A1 (en) * 2002-01-25 2003-07-31 Sporlan Valve Company Molded core filter drier with filter media molded to core for use in heat pump systems
US20030140793A1 (en) * 2002-01-25 2003-07-31 Sporlan Valve Company Molded core filter drier with filter media molded to core
US7132011B2 (en) * 2003-09-02 2006-11-07 Entegris, Inc. Reactive gas filter
US7278401B1 (en) * 2004-10-29 2007-10-09 Walbro Engine Management, L.L.C. Fuel pressure regulator housing
US20080005919A1 (en) * 2006-07-10 2008-01-10 Brown Jerome R In-line dryer
US20090288427A1 (en) * 2008-05-21 2009-11-26 Raytheon Company Isothermal gas supply and method for minimizing the temperature excursion of a gas mixture released therefrom
US20150083425A1 (en) * 2012-05-08 2015-03-26 Release Energy Pty Ltd Inline non-targeted component removal
US20150298040A1 (en) * 2012-12-14 2015-10-22 Entegris, Inc. Gas Purification Filter Unit

Also Published As

Publication number Publication date
ES2547957A1 (en) 2015-10-09
PT3147572T (en) 2021-04-19
ES2879048T3 (en) 2021-11-19
ES2547957B1 (en) 2016-04-29
EP3147572A4 (en) 2018-03-07
WO2015155388A1 (en) 2015-10-15
MX362395B (en) 2019-01-15
EP3147572B1 (en) 2021-01-13
EP3147572A1 (en) 2017-03-29
MX2016012807A (en) 2017-01-05

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