US20130078583A1 - Heat Recycling System for a High-Temperature Exhaust Gas - Google Patents

Heat Recycling System for a High-Temperature Exhaust Gas Download PDF

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US20130078583A1
US20130078583A1 US13/241,913 US201113241913A US2013078583A1 US 20130078583 A1 US20130078583 A1 US 20130078583A1 US 201113241913 A US201113241913 A US 201113241913A US 2013078583 A1 US2013078583 A1 US 2013078583A1
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Prior art keywords
gas
check valve
store tank
burning
exhaust gas
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Abandoned
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US13/241,913
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Yu-Po Lee
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Priority to US13/241,913 priority Critical patent/US20130078583A1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L11/00Arrangements of valves or dampers after the fire
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • F23L15/02Arrangements of regenerators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L17/00Inducing draught; Tops for chimneys or ventilating shafts; Terminals for flues
    • F23L17/005Inducing draught; Tops for chimneys or ventilating shafts; Terminals for flues using fans
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/04Regulating fuel supply conjointly with air supply and with draught
    • F23N1/042Regulating fuel supply conjointly with air supply and with draught using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2237/00Controlling
    • F23N2237/02Controlling two or more burners
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2237/00Controlling
    • F23N2237/20Controlling one or more bypass conduits
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Definitions

  • the present invention relates to a heat recycling system for a high-temperature exhaust gas, and more particularly to the high-temperature exhaust gas discharged by the body and recycled its heat energy by a storing device so as to discharge a lower-temperature exhaust gas, after the storing device absorbs the heat energy fully and introduces a combustion gas, the heat recycling system warns a room-temperature gas so that the room-temperature gas is introduced into a combustion space of a body.
  • a conventional burning system contains a body A, a burning unit B and a storing unit C.
  • the body A includes a combustion space A 1 to be a heat exchange area.
  • the burning unit B is comprised of at least one pair of first machine B 1 and second machine B 2 , and the at least one pair of first machine B 1 and second machine B 2 , are fixed on two sides of the body A individually to be started on and off reciprocately to supply burning fuels (Liquefied Petroleum Gas LPG or Liquefied Natural Gas LNG) to the combustion space A 1 of the body A.
  • a power of the at least one pair of first machine B 1 and second machine B 2 is a fuel calculated by a unit of kg or m 3 /h in a sufficient burning condition and is a heat output (kw/h or kcal/h).
  • the storing unit C is disposed on two sides of the body A and is comprised of a first store cylinder C 1 , a first blower C 2 , a second store cylinder C 3 , and a second blower C 4 , wherein between the first store cylinder C 1 and the first machine B 1 is defined a first switch valve C 5 , and the first store cylinder C 1 is connected with a first check valve C 11 , between the second store cylinder C 3 and the second machine B 2 is defined a second switch valve C 6 , and the second store cylinder C 3 is coupled with a second check valve C 31 .
  • the second machine B 2 When the first machine B 1 of the burning unit B is started to supply the burning fuel to the combustion space A 1 of the body A, the second machine B 2 is turned off and stops a supply of the burning fuels.
  • the second blower C 4 of the storing unit C is started so that a heat energy stored by the second store cylinder C 3 is supplied to the first machine B 1 of the body A via the second machine B 2 to be burned, and the first switch valve C 5 of the storing unit C is started simultaneously so that the heat energy resulting from the body A is discharged and stored in the first store cylinder C 1 .
  • the first machine B 1 is turned off and stops the supply of the burning fuels.
  • the first blower C 2 of the storing unit C is started so that the heat energy stored by the first store cylinder C 1 is supplied to the second machine B 2 of the body A to be burned further, and the second switch valve C 6 of the storing unit C is turned on so that the heat energy resulting from the body A is discharged and stored in the second store cylinder C 3 .
  • the first machine B 1 is turned on by controlling the heat energy stored in the first store cylinder C 1 , and when the heat energy is stored in the first store cylinder C 1 fully, the supply of the burning fuels from the first machine B 1 to the body A is stopped, while the first machine B 1 is turned off by controlling the heat energy stored in the second store cylinder C 3 , and when the heat energy is stored in the second store cylinder C 3 fully, the supply of the burning fuels from the second machine B 2 to the body A is stopped.
  • the burning unit B is comprised of a pair of the first machine B 1 and the second machine B 2 to turn on and off interactively, thus having high machine purchase cost.
  • the burning system has a burning operation and a storing operation interactively so that the first machine B 1 and the second machine B 2 are turned on and off interactively to supply the burning fuels (around 2-3 minutes/per turn on-off operation), but such a turned on-off operation will waste the burning fuels during a temperature increasing period of the machine. For example, if the temperature increasing period of the machine is 3 minutes, the burring fuels will be burned more than 5 seconds.
  • the first machine B 1 and the second machine B 2 are turned on and off interactively to supply the burning fuels, so an extreme heat impacts the machine to lower machine's life.
  • the first machine B 1 and the second machine B 2 are turned on and off interactively to supply the burning fuels, hence an extreme temperature change happens on the machine, and the first store cylinder C 1 and the second store cylinder C 3 of the storing unit C have to be fixed close to the body A, accordingly a heat storing area of the body A is limited to have a poor combustion space.
  • a pipeline is applied to introduce the exhaust gas outward and to feed the heat energy, therefore the heat energy is maintained difficultly to cause heat consumption greatly.
  • the present invention has arisen to mitigate and/or obviate the afore-described disadvantages.
  • the primary object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of discharging the high-temperature exhaust gas by a body, and after a storing device absorbs a heat energy fully and introduces a combustion gas, the heat recycling system warns a room-temperature gas so that the room-temperature gas is introduced into a combustion space of the body.
  • Secondary object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas in which only at least one burning device is provided to supply burning fuels constantly, and the storing device is capable of supplying a recycled heat energy resulting from an exhaust gas so that a burning temperature of the combustion space of the body keeps at a high temperature to improve an extreme heat impact on a machine.
  • Third object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas in which the at least one burning device is capable of providing 2N ⁇ 10 thousand kcal of heat energy if the body requires N ⁇ 10 thousand kcal of heat energy so that a burning system is operated well at a lower cost.
  • Fourth object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of enhancing burning fuels effectively to prevent from fuel consumption and is capable of keeping a burning temperature of the combustion space of at the high temperature to save fuel cost.
  • Fifth object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of preventing from the extreme heat impact on a machine to prolong the machine's life.
  • Another object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of preventing from a temperature change so that a first store tank and a second store tank have not to be fixed close to the body, and the second store tank is provided in a large size to increase heat storing and burning efficiency.
  • a heat recycling system for a high-temperature exhaust gas contains a body having a combustion space, at least one burning device disposed beside the body, and a storing device;
  • the combustion space of the body is connected with an exhaust pipe
  • the burning device is coupled with a heat recycling blower and a gas control valve;
  • the storing device is secured on a distal end of the exhaust pipe of the body and is comprised of a second control valve, a first store tank, and a second store tank;
  • the second control valve is disposed on the distal end of the exhaust pipe of the body and includes two output ends which connect with a gas guiding tube and a second guiding tube respectively;
  • the first store tank is coupled with the gas guiding tube and is connected with a first check valve and a second check valve, the gas check valve is coupled with a first gas-exhausting blower, and between the first store tank and the gas control valve is defined a first hose;
  • a second store tank is connected with the second guiding tube and is coupled with a third check valve and a fourth check valve, the fourth check valve connects with a second gas-exhausting blower, between the second store tank and the gas control valve is defined a second hose.
  • FIG. 1 is a block diagram of a conventional burning system
  • FIG. 2 is a block diagram showing the assembly of a heat recycling system for a high-temperature exhaust gas according to a preferred embodiment of the present invention.
  • a heat recycling system for a high-temperature exhaust gas comprises: a body 1 having a combustion space 11 , at least one burning device 2 , and a storing device 3 .
  • the body 1 includes the combustion space 11 connected with an exhaust pipe 111 .
  • the burning device 2 is fixed beside the body 1 to supply burning fuels (Liquefied Petroleum Gas LPG or Liquefied Natural Gas LNG) to the combustion space 11 of the body 1 and is coupled with a heat recycling blower 21 , and the heat recycling blower 21 is connected with a gas control valve 22 ; a power of the burning device 2 is a fuel calculated by a unit of kg or m 3 /h in a sufficient burning condition and is a heat output (kw/h or kcal/h).
  • burning fuels Liiquefied Petroleum Gas LPG or Liquefied Natural Gas LNG
  • the storing device 3 is secured on a distal end of the exhaust pipe 111 of the body 1 and is comprised of a second control valve 31 , a first store tank 32 , and a second store tank 33 ;
  • the second control valve 31 is disposed on the distal end of the exhaust pipe 111 of the body 1 and includes two output ends which connect with a gas guiding tube 311 and a second guiding tube 312 respectively;
  • the first store tank 32 is coupled with an outlet end of the gas guiding tube 311 and is connected with a first check valve 321 and a second check valve 322 , an outlet end of the second check valve 322 is coupled with a first gas-exhausting blower 323 , and between the first store tank 32 and the gas control valve 22 is defined a first hose 34 ;
  • the second store tank 33 is connected with the second guiding tube 312 and is coupled with a third check valve 331 and a fourth check valve 332 , an outlet end of the fourth check valve 332 connects with a second gas-ex
  • the body 1 of the heat recycling system discharges the high-temperature exhaust gas, and a heat energy of the high-temperature exhaust gas is recycled by the heat recycling blower 21 , and then a low-temperature exhaust gas is discharged; after the first store tank 32 and the second store tank 33 of the storing device 3 absorb a heat completely, a normal combustion gas is introduced via the first check valve 321 and the third check valve 331 so that a room-temperature gas is warmed and introduced into the combustion space 11 of the body 1 .
  • the burning device 2 is started to supply the burning fuels (LPG or LNG) to the combustion space 11 of the body 1 , the high-temperature exhaust gas resulting from burning is discharged from the exhaust pipe 111 of the combustion space 11 to flow into the first store tank 32 via the second control valve 31 , and then the first store tank 32 discharges a lower-temperature exhaust gas outward through the second check valve 322 and the first gas-exhausting blower 323 .
  • LPG burning fuels
  • LNG high-temperature exhaust gas resulting from burning
  • the first store tank 32 When the first store tank 32 discharges the lower-temperature exhaust gas and stores a heat energy fully, it introduces the normal combustion gas by using the first check valve 321 , and a recycled heat energy is introduced into the burning device 2 through the first hose 34 , the gas control valve 22 , and the heat recycling blower 21 , thereby supplying the combustion gas to the combustion space 11 .
  • the second store tank 33 discharges the lower-temperature exhaust gas outward through the fourth check valve 332 and the second gas-exhausting blower 333 .
  • the second store tank 33 introduces the normal combustion gas via the third check valve 331 , and the recycled heat energy is introduced into the burning device 2 via the second hose 35 , the gas control valve 22 , and the heat recycling blower 21 , thus supplying the combustion gas to the combustion space 11 .
  • an operating temperature (flame temperature) of the melting stove is 1,250° C.
  • a discharging temperature of the exhaust gas is 900° C.
  • a discharging temperature of the exhaust gas of the first gas-exhausting blower 323 and the second gas-exhausting blower 333 is 250° C.
  • a required temperature is 1,250° C. (an operating temperature) ⁇ 30° C. (an inflow temperature/the room temperature) which is equal to 1,220° C.
  • the required temperature is 1,250° C. (the operating temperature) ⁇ 605° C. (the inflow temperature/a heat recycle) which is equal to 645° C.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Feeding And Controlling Fuel (AREA)

Abstract

A heat recycling system for a high-temperature exhaust gas contains a body having a combustion space, at least one burning device, and a storing device; characterized in that: the combustion space is connected with an exhaust pipe; the burning device is coupled with a heat recycling blower and a gas control valve; the storing device is secured on a distal end of the exhaust pipe and is comprised of a second control valve, a first store tank, and a second store tank; the second control valve is disposed on the exhaust pipe of the body and includes two output ends which connect with a gas guiding tube and a second guiding tube respectively; the first store tank is coupled with the gas guiding tube and is connected with a first check valve and a second check valve, the gas check valve is coupled with a first gas-exhausting blower.

Description

    BACKGROUND OF THE INVENTION
  • 1. Field of the Invention
  • The present invention relates to a heat recycling system for a high-temperature exhaust gas, and more particularly to the high-temperature exhaust gas discharged by the body and recycled its heat energy by a storing device so as to discharge a lower-temperature exhaust gas, after the storing device absorbs the heat energy fully and introduces a combustion gas, the heat recycling system warns a room-temperature gas so that the room-temperature gas is introduced into a combustion space of a body.
  • 2. Description of the Prior Art
  • Referring to FIG. 1, a conventional burning system contains a body A, a burning unit B and a storing unit C.
  • The body A includes a combustion space A1 to be a heat exchange area.
  • The burning unit B is comprised of at least one pair of first machine B1 and second machine B2, and the at least one pair of first machine B1 and second machine B2, are fixed on two sides of the body A individually to be started on and off reciprocately to supply burning fuels (Liquefied Petroleum Gas LPG or Liquefied Natural Gas LNG) to the combustion space A1 of the body A. A power of the at least one pair of first machine B1 and second machine B2, is a fuel calculated by a unit of kg or m3/h in a sufficient burning condition and is a heat output (kw/h or kcal/h).
  • The storing unit C is disposed on two sides of the body A and is comprised of a first store cylinder C1, a first blower C2, a second store cylinder C3, and a second blower C4, wherein between the first store cylinder C1 and the first machine B1 is defined a first switch valve C5, and the first store cylinder C1 is connected with a first check valve C11, between the second store cylinder C3 and the second machine B2 is defined a second switch valve C6, and the second store cylinder C3 is coupled with a second check valve C31.
  • When the first machine B1 of the burning unit B is started to supply the burning fuel to the combustion space A1 of the body A, the second machine B2 is turned off and stops a supply of the burning fuels. During an operation of the first machine B1, the second blower C4 of the storing unit C is started so that a heat energy stored by the second store cylinder C3 is supplied to the first machine B1 of the body A via the second machine B2 to be burned, and the first switch valve C5 of the storing unit C is started simultaneously so that the heat energy resulting from the body A is discharged and stored in the first store cylinder C1.
  • While the second machine B2 of the burning unit B is turned on to supply the burning fuels to the combustion space A1 of the body A, the first machine B1 is turned off and stops the supply of the burning fuels. During an operation of the second machine B2, the first blower C2 of the storing unit C is started so that the heat energy stored by the first store cylinder C1 is supplied to the second machine B2 of the body A to be burned further, and the second switch valve C6 of the storing unit C is turned on so that the heat energy resulting from the body A is discharged and stored in the second store cylinder C3.
  • The first machine B1 is turned on by controlling the heat energy stored in the first store cylinder C1, and when the heat energy is stored in the first store cylinder C1 fully, the supply of the burning fuels from the first machine B1 to the body A is stopped, while the first machine B1 is turned off by controlling the heat energy stored in the second store cylinder C3, and when the heat energy is stored in the second store cylinder C3 fully, the supply of the burning fuels from the second machine B2 to the body A is stopped.
  • However, the conventional burning system still has the following defects:
  • 1. If a required heat energy of the body A is N×10 thousand kcal, the heat energy supplied from the machine is 2N×10 thousand kcal to operate the burning system, the burning unit B is comprised of a pair of the first machine B1 and the second machine B2 to turn on and off interactively, thus having high machine purchase cost.
  • 2. The burning system has a burning operation and a storing operation interactively so that the first machine B1 and the second machine B2 are turned on and off interactively to supply the burning fuels (around 2-3 minutes/per turn on-off operation), but such a turned on-off operation will waste the burning fuels during a temperature increasing period of the machine. For example, if the temperature increasing period of the machine is 3 minutes, the burring fuels will be burned more than 5 seconds.
  • 3. The first machine B1 and the second machine B2 are turned on and off interactively to supply the burning fuels, so an extreme heat impacts the machine to lower machine's life.
  • 4. The first machine B1 and the second machine B2 are turned on and off interactively to supply the burning fuels, hence an extreme temperature change happens on the machine, and the first store cylinder C1 and the second store cylinder C3 of the storing unit C have to be fixed close to the body A, accordingly a heat storing area of the body A is limited to have a poor combustion space.
  • 5. A pipeline is applied to introduce the exhaust gas outward and to feed the heat energy, therefore the heat energy is maintained difficultly to cause heat consumption greatly.
  • 6. The related components to flame the burning fuels (LPG or LNG) are used overly to lower a service life easily.
  • However, such a conventional dental floss brush can not be used to eliminate pieces of a tongue coating of a tongue.
  • The present invention has arisen to mitigate and/or obviate the afore-described disadvantages.
  • SUMMARY OF THE INVENTION
  • The primary object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of discharging the high-temperature exhaust gas by a body, and after a storing device absorbs a heat energy fully and introduces a combustion gas, the heat recycling system warns a room-temperature gas so that the room-temperature gas is introduced into a combustion space of the body.
  • Secondary object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas in which only at least one burning device is provided to supply burning fuels constantly, and the storing device is capable of supplying a recycled heat energy resulting from an exhaust gas so that a burning temperature of the combustion space of the body keeps at a high temperature to improve an extreme heat impact on a machine.
  • Third object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas in which the at least one burning device is capable of providing 2N×10 thousand kcal of heat energy if the body requires N×10 thousand kcal of heat energy so that a burning system is operated well at a lower cost.
  • Fourth object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of enhancing burning fuels effectively to prevent from fuel consumption and is capable of keeping a burning temperature of the combustion space of at the high temperature to save fuel cost.
  • Fifth object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of preventing from the extreme heat impact on a machine to prolong the machine's life.
  • Another object of the present invention is to provide a heat recycling system for a high-temperature exhaust gas that is capable of preventing from a temperature change so that a first store tank and a second store tank have not to be fixed close to the body, and the second store tank is provided in a large size to increase heat storing and burning efficiency.
  • A heat recycling system for a high-temperature exhaust gas contains a body having a combustion space, at least one burning device disposed beside the body, and a storing device;
  • characterized in that:
  • the combustion space of the body is connected with an exhaust pipe;
  • the burning device is coupled with a heat recycling blower and a gas control valve;
  • the storing device is secured on a distal end of the exhaust pipe of the body and is comprised of a second control valve, a first store tank, and a second store tank; the second control valve is disposed on the distal end of the exhaust pipe of the body and includes two output ends which connect with a gas guiding tube and a second guiding tube respectively; the first store tank is coupled with the gas guiding tube and is connected with a first check valve and a second check valve, the gas check valve is coupled with a first gas-exhausting blower, and between the first store tank and the gas control valve is defined a first hose; a second store tank is connected with the second guiding tube and is coupled with a third check valve and a fourth check valve, the fourth check valve connects with a second gas-exhausting blower, between the second store tank and the gas control valve is defined a second hose.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 is a block diagram of a conventional burning system;
  • FIG. 2 is a block diagram showing the assembly of a heat recycling system for a high-temperature exhaust gas according to a preferred embodiment of the present invention.
  • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • The present invention will be clearer from the following description when viewed together with the accompanying drawings, which show, for purpose of illustrations only, the preferred embodiment in accordance with the present invention.
  • With reference to FIG. 2, a heat recycling system for a high-temperature exhaust gas according to a preferred embodiment of the present invention comprises: a body 1 having a combustion space 11, at least one burning device 2, and a storing device 3.
  • The body 1 includes the combustion space 11 connected with an exhaust pipe 111.
  • The burning device 2 is fixed beside the body 1 to supply burning fuels (Liquefied Petroleum Gas LPG or Liquefied Natural Gas LNG) to the combustion space 11 of the body 1 and is coupled with a heat recycling blower 21, and the heat recycling blower 21 is connected with a gas control valve 22; a power of the burning device 2 is a fuel calculated by a unit of kg or m3/h in a sufficient burning condition and is a heat output (kw/h or kcal/h).
  • The storing device 3 is secured on a distal end of the exhaust pipe 111 of the body 1 and is comprised of a second control valve 31, a first store tank 32, and a second store tank 33; the second control valve 31 is disposed on the distal end of the exhaust pipe 111 of the body 1 and includes two output ends which connect with a gas guiding tube 311 and a second guiding tube 312 respectively; the first store tank 32 is coupled with an outlet end of the gas guiding tube 311 and is connected with a first check valve 321 and a second check valve 322, an outlet end of the second check valve 322 is coupled with a first gas-exhausting blower 323, and between the first store tank 32 and the gas control valve 22 is defined a first hose 34; the second store tank 33 is connected with the second guiding tube 312 and is coupled with a third check valve 331 and a fourth check valve 332, an outlet end of the fourth check valve 332 connects with a second gas-exhausting blower 333, between the second store tank 33 and the gas control valve 22 is defined a second hose 35.
  • The body 1 of the heat recycling system discharges the high-temperature exhaust gas, and a heat energy of the high-temperature exhaust gas is recycled by the heat recycling blower 21, and then a low-temperature exhaust gas is discharged; after the first store tank 32 and the second store tank 33 of the storing device 3 absorb a heat completely, a normal combustion gas is introduced via the first check valve 321 and the third check valve 331 so that a room-temperature gas is warmed and introduced into the combustion space 11 of the body 1.
  • In operation, the burning device 2 is started to supply the burning fuels (LPG or LNG) to the combustion space 11 of the body 1, the high-temperature exhaust gas resulting from burning is discharged from the exhaust pipe 111 of the combustion space 11 to flow into the first store tank 32 via the second control valve 31, and then the first store tank 32 discharges a lower-temperature exhaust gas outward through the second check valve 322 and the first gas-exhausting blower 323. When the first store tank 32 discharges the lower-temperature exhaust gas and stores a heat energy fully, it introduces the normal combustion gas by using the first check valve 321, and a recycled heat energy is introduced into the burning device 2 through the first hose 34, the gas control valve 22, and the heat recycling blower 21, thereby supplying the combustion gas to the combustion space 11.
  • When the high-temperature exhaust gas flows into the second store tank 33 via the second control valve 31, the second store tank 33 discharges the lower-temperature exhaust gas outward through the fourth check valve 332 and the second gas-exhausting blower 333. After the second store tank 33 discharges the lower-temperature exhaust gas and stores the heat energy fully, it introduces the normal combustion gas via the third check valve 331, and the recycled heat energy is introduced into the burning device 2 via the second hose 35, the gas control valve 22, and the heat recycling blower 21, thus supplying the combustion gas to the combustion space 11.
  • When the heat recycling system of the present invention is used in an aluminum alloy melting stove, wherein
  • an operating temperature (flame temperature) of the melting stove is 1,250° C., and a discharging temperature of the exhaust gas is 900° C., after the discharging temperature of the exhaust gas at 900° C. is recycled through the first store tank 32 and the second store tank 33, a discharging temperature of the exhaust gas of the first gas-exhausting blower 323 and the second gas-exhausting blower 333 is 250° C., and a recycling temperature of the first store tank 32 and the second store tank 33 is 650° C. (i.e., 900° C.−250° C.=·650° C.).
  • The room-temperature gas flows into the burning device 2 and the combustion space 11 of the body 1 through the first check valve 321, the third check valve 331, the first store tank 32, and the second store tank 33 in order, and the heat energy absorbed by the storing device 3 is 575° C., i.e., (900° C.+250° C.)/2=575° C., so the 575° C. is a temperature supplied by the first store tank 32 and the second store tank 33, wherein 30° C. (a room temperature)+575° C.=605° C., so the 605° C. is an gas temperature which flows into the combustion space 11 of the body 1 to flame.
  • When a conventional melting stove is not equipped with the heat recycling system of the present invention, a required temperature is 1,250° C. (an operating temperature)−30° C. (an inflow temperature/the room temperature) which is equal to 1,220° C.
  • After the melting stove is equipped with the heat recycling system of the present invention, the required temperature is 1,250° C. (the operating temperature)−605° C. (the inflow temperature/a heat recycle) which is equal to 645° C.
  • Accordingly, a heat recycle effect of the heat recycling system of the present invention is 645° C.×(100%−35%)=419.25° C. (an estimated heat recycle loss is 35%), 100%−((1,220° C.−419.25° C.)/1,220° C.)=34.36%.
  • While we have shown and described various embodiments in accordance with the present invention, it is clear to those skilled in the art that further embodiments may be made without departing from the scope of the present invention.

Claims (3)

What is claimed is:
1. A heat recycling system for a high-temperature exhaust gas comprising a body having a combustion space, at least one burning device disposed beside the body, and a storing device;
characterized in that:
the combustion space of the body is connected with an exhaust pipe;
the burning device is coupled with a heat recycling blower and a gas control valve;
the storing device is secured on a distal end of the exhaust pipe of the body and is comprised of a second control valve, a first store tank, and a second store tank; the second control valve is disposed on the distal end of the exhaust pipe of the body and includes two output ends which connect with a gas guiding tube and a second guiding tube respectively; the first store tank is coupled with the gas guiding tube and is connected with a first check valve and a second check valve, the gas check valve is coupled with a first gas-exhausting blower, and between the first store tank and the gas control valve is defined a first hose; a second store tank is connected with the second guiding tube and is coupled with a third check valve and a fourth check valve, the fourth check valve connects with a second gas-exhausting blower, between the second store tank and the gas control valve is defined a second hose.
2. The heat recycling system for the high-temperature exhaust gas as claimed in claim 1, wherein the first check valve and the third check valve are used to introduce a combustion gas into the first store tank and the second store tank respectively.
3. The heat recycling system for the high-temperature exhaust gas as claimed in claim 1, wherein the second check valve and the fourth check valve are used to supply a low-temperature exhaust gas to the first store tank and the second store tank respectively
US13/241,913 2011-09-23 2011-09-23 Heat Recycling System for a High-Temperature Exhaust Gas Abandoned US20130078583A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2158095A (en) * 1936-03-17 1939-05-16 Emil A Vierow Regenerative furnace
US2723842A (en) * 1951-03-15 1955-11-15 Morgan Construction Co Regenerative furnace apparatus having flue gas separators
US2715893A (en) * 1951-09-20 1955-08-23 Hingst Rudolf Regenerator firing plant
US2944806A (en) * 1956-01-23 1960-07-12 Power Gas Ltd Heating gases and vapours
US2927847A (en) * 1956-03-02 1960-03-08 Gas Council Heating gases and vapours
US4412509A (en) * 1973-06-11 1983-11-01 Black Robert B Energy conversion system and components thereof
US4180128A (en) * 1975-12-18 1979-12-25 John J. Fallon, Jr. Multiple furnace waste heat recovery system
US4299561A (en) * 1980-03-18 1981-11-10 Stokes Keith J Recovery of heat from flue gas
US4424857A (en) * 1981-10-01 1984-01-10 Linde Aktiengesellschaft Method for reversing two regenerators
US4666403A (en) * 1986-08-06 1987-05-19 Morgan Construction Company Air preheating system for continuous fired furnace
US5299630A (en) * 1991-11-09 1994-04-05 Oskar Schatz Method of rapidly heating a mass to an operative temperature, in particular a vehicle engine during cold starting
US5740683A (en) * 1997-03-27 1998-04-21 Praxair Technology, Inc. Cryogenic rectification regenerator system
US5802872A (en) * 1997-07-30 1998-09-08 Praxair Technology, Inc. Cryogenic air separation with combined prepurifier and regenerators
US5950455A (en) * 1998-04-01 1999-09-14 Praxair Technology, Inc. Cryogenic air separation system for feed air flow disturbances
US6863523B2 (en) * 2002-06-28 2005-03-08 Ppl Corporation Crossflow air heater bypass
US7097210B2 (en) * 2003-09-30 2006-08-29 Spx Corporation Method and apparatus for providing a transition connector to introduce outside air and vent flue for boiler combustion
US7708963B2 (en) * 2004-05-07 2010-05-04 Johannes Schedler Method and apparatus for treating waste gas flows laden with aerosol and dust
US20090095440A1 (en) * 2006-02-25 2009-04-16 Manfred Gietz Method for optimised operation of an air preheater and air preheater

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