WO2009030987A2 - Cooling arrangement of a gas turbine air inlet - Google Patents

Cooling arrangement of a gas turbine air inlet Download PDF

Info

Publication number
WO2009030987A2
WO2009030987A2 PCT/IB2008/000353 IB2008000353W WO2009030987A2 WO 2009030987 A2 WO2009030987 A2 WO 2009030987A2 IB 2008000353 W IB2008000353 W IB 2008000353W WO 2009030987 A2 WO2009030987 A2 WO 2009030987A2
Authority
WO
WIPO (PCT)
Prior art keywords
gas turbine
cooling
arrangement
refrigeration
water
Prior art date
Application number
PCT/IB2008/000353
Other languages
French (fr)
Other versions
WO2009030987A3 (en
Inventor
Robert George Howell
Original Assignee
Dubai Aluminium Company Limited
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 Dubai Aluminium Company Limited filed Critical Dubai Aluminium Company Limited
Publication of WO2009030987A2 publication Critical patent/WO2009030987A2/en
Publication of WO2009030987A3 publication Critical patent/WO2009030987A3/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C7/00Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
    • F02C7/12Cooling of plants
    • F02C7/14Cooling of plants of fluids in the plant, e.g. lubricant or fuel
    • F02C7/141Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid
    • F02C7/143Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid before or between the compressor stages
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C1/00Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
    • F02C1/04Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
    • F02C1/05Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly characterised by the type or source of heat, e.g. using nuclear or solar energy
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2260/00Function
    • F05D2260/20Heat transfer, e.g. cooling
    • F05D2260/207Heat transfer, e.g. cooling using a phase changing mass, e.g. heat absorbing by melting or boiling
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Definitions

  • This invention relates to a cooling arrangement and apparatus. More particularly, this invention relates to a cooling arrangement and apparatus for cooling the inlet air of gas turbines, particularly gas turbines for use in the generation of electricity within single site aluminium smelters utilizing the available waste heat produced by the smelting process or associated processes .
  • Gas turbines are widely used in the generation of electricity where gas or liquid fuel is available. Steam turbines are used with gas turbines either in combined cycle or separately using the waste heat from the gas turbine to produce more power.
  • steam turbines using nuclear, gas or coal fuel for producing heat for its boiler systems are used to generate electricity for towns, cities or the like.
  • gas turbines are often used where plants or factories require on-site electricity generating facilities.
  • a plant such as an aluminium smelting plant
  • a single site smelter gas turbines are well suited for the production of electricity at single site smelters, this type of turbine is not without its disadvantages.
  • One of the main disadvantages of a gas turbine is that it is very sensitive to ambient temperature variations. A gas turbine will deliver more power in low ambient temperature conditions and deliver less power in high ambient temperature conditions.
  • a cooling arrangement for cooling inlet air of a gas turbine including cooling means and a heat exchanger located in an air inlet path of the gas turbine.
  • the cooling arrangement includes an absorptive refrigeration means.
  • the refrigeration means is preferably a Lithium Bromide and water type absorptive refrigeration means.
  • absorptive refrigeration means any suitable type may be used. Because absorption refrigeration requires low grade heat as an energy source to function, it is well suited for cooling purposes in a plant such as an aluminium smelter where there is an abundance of hot waste gases.
  • the refrigeration means preferably includes a plurality of absorptive refrigeration units, each unit being supplied by hot water which has been heated by hot gases from a fume treatment plant in an aluminium smelting plant; a chilled water circuit wherein water is circulated through the refrigeration units during which time it is chilled, to a gas turbine air inlet and back to the refrigeration units.
  • the cooling arrangement may further include a cooling water supply and return circuit, via a cooling tower arrangement for purposes of condensing water used during the absorption process in the absorptive refrigeration units.
  • the cooling water is used to condense the working fluid such as Lithium Bromide during the absorption process in the absorptive refrigeration units.
  • the cooling means may include a plurality of absorptive refrigeration units, each unit being supplied by hot water which has been heated, in use, by hot gases from a fume treatment plant in an aluminium smelting plant; and a chilled water circuit wherein water is circulated through the refrigeration units during which time it is chilled, in use, to a heat exchanger located at a gas turbine air inlet and back to the refrigeration units.
  • the waste heat produced by the aluminium smelting process may be recovered for absorption cooling from the power production, casting process, the anode baking kilns or the electrolytic reduction cells.
  • a process for cooling gas turbine inlet air including the steps of lowering the temperature of a fluid by means of absorptive refrigeration and using the fluid to cool the gas turbine inlet air.
  • the chilled water from the absorption coolers may also provide air conditioning comfort cooling for the plant personnel.
  • a gas turbine including a cooling arrangement as described in the specification.
  • an aluminium smelting plant including at least one gas turbine as described herein.
  • the process may include the step of using waste hot gases to energize the absorptive refrigeration means.
  • a cooling arrangement 10 is shown to include an absorption plant 12 including seven absorptive refrigeration units (not shown).
  • the absorptive refrigeration units are of the Lithium Bromide and water type.
  • the absorptive refrigeration units are energized by via twenty four heat recovery points 14.
  • the arrangement 10 is installed in an aluminium smelting plant (not shown) and the heat recovery points 14 are located near fume treatment plants (not shown).
  • hot gases from aluminium smelting cells are treated - typically, by removing hydrogen fluoride by dry scrubbing with alumina.
  • a water supply and return circuit 18 contains water which absorbs heat from the hot gases at the heat recovery points 14 and which is pumped at approximately 120 degrees Celsius via supply line 18.1 to the absorption plant 12 where the heated water energizes the absorptive refrigeration units (not shown). The water is then returned via return line 18.2 at approximately 90 degrees Celsius to the heat recovery points and the cycle is repeated.
  • the fumes exiting the heat recovery are cooled from 130 C to around 100 C.
  • the adsorption efficiency of the alumina scrubbing media is consequently enhanced thus hydrogen fluoride recovery is improved in the order of 25%, reducing harmful emissions from the potroom fume treatment plants.
  • Hot exhaust fumes 17 exit the heat recovery points 14 and are scrubbed before being expelled to atmosphere.
  • a chilling water supply and return circuit 20 contains water which is cooled (or chilled) in the absorption plant 12 to about 15 degrees Celsius and which is then pumped via supply line 20.1 to four gas turbine heat exchangers 22. The water is then returned via return line 20.2 at about 25 degrees Celsius to the absorption plant 12 and the cycle is repeated.
  • a cooling tower arrangement 28 is provided for lowering the temperature of absorption plant cooling water.
  • the cooling water is used to condense the working fluid of the absorption refrigeration units in the normal operation of these units.
  • a cooling water supply and return circuit 30 contains cooling water which pumped via supply line 30.1 to the absorption plant 12 at about 34 degrees Celsius and returned via return line 30.2 at about 43 degrees Celsius and the cycle is repeated.
  • Cooling the gases from the electrolytic reduction cells improves the adsorption ability of alumina scrubbing media thus improving hydrogen fluoride recovery. Cooling the gases entering the fume treatment plants from the electrolytic reduction cells allows operators to increase potline amperage without detrimental effect on the fume treatment plants.
  • Chilled water from the absorption refrigeration process may be used to provide comfort cooling [air conditioning] for plant personnel.
  • Waste heat for absorption cooling within an aluminium smelter may be recovered from power production, casting process, anode baking kilns, desalination or reduction cells.
  • Cooling the gases from the electrolytic reduction cells extends filter bag life.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Turbine Rotor Nozzle Sealing (AREA)

Abstract

The invention relates to a cooling arrangement (10) for cooling inlet air for a gas turbine, including refrigeration means (12) and a heat exchanger (22) located in an air inlet path of the gas turbine.

Description

COOLING ARRANGEMENT
FIELD OF THE INVENTION
This invention relates to a cooling arrangement and apparatus. More particularly, this invention relates to a cooling arrangement and apparatus for cooling the inlet air of gas turbines, particularly gas turbines for use in the generation of electricity within single site aluminium smelters utilizing the available waste heat produced by the smelting process or associated processes .
BACKGROUND TO THE INVENTION
Gas turbines are widely used in the generation of electricity where gas or liquid fuel is available. Steam turbines are used with gas turbines either in combined cycle or separately using the waste heat from the gas turbine to produce more power.
Generally, steam turbines, using nuclear, gas or coal fuel for producing heat for its boiler systems are used to generate electricity for towns, cities or the like.
On the other hand, gas turbines are often used where plants or factories require on-site electricity generating facilities. Such is the case in many aluminium smelting plants over the world because the high electricity requirements for this type of plant usually dictate these plants are located near an abundant source of energy such as natural gas, oil, coal, nuclear or hydroelectric.
Where a plant, such as an aluminium smelting plant, has its own on-site electricity generating plant, it is commonly referred to a "single site smelter". Although gas turbines are well suited for the production of electricity at single site smelters, this type of turbine is not without its disadvantages. One of the main disadvantages of a gas turbine is that it is very sensitive to ambient temperature variations. A gas turbine will deliver more power in low ambient temperature conditions and deliver less power in high ambient temperature conditions.
This is mainly due to the reliance of a gas turbine on air density in its operation. It will therefore be appreciated that in hot climates, gas turbines are less efficient than in cold climates.
OBJECT OF THE INVENTION
It is accordingly an object of the invention to provide a means for cooling inlet air for a gas turbine for making the gas turbine more efficient in hot ambient temperature conditions utilizing available waste heat.
SUMMARY OF THE INVENTION
According to a first aspect of the invention, there is provided a cooling arrangement for cooling inlet air of a gas turbine including cooling means and a heat exchanger located in an air inlet path of the gas turbine.
In a preferred form of the invention, the cooling arrangement includes an absorptive refrigeration means. The refrigeration means is preferably a Lithium Bromide and water type absorptive refrigeration means.
It will be appreciated that any suitable type of absorptive refrigeration means may be used. Because absorption refrigeration requires low grade heat as an energy source to function, it is well suited for cooling purposes in a plant such as an aluminium smelter where there is an abundance of hot waste gases.
The refrigeration means preferably includes a plurality of absorptive refrigeration units, each unit being supplied by hot water which has been heated by hot gases from a fume treatment plant in an aluminium smelting plant; a chilled water circuit wherein water is circulated through the refrigeration units during which time it is chilled, to a gas turbine air inlet and back to the refrigeration units.
The cooling arrangement may further include a cooling water supply and return circuit, via a cooling tower arrangement for purposes of condensing water used during the absorption process in the absorptive refrigeration units.
The cooling water is used to condense the working fluid such as Lithium Bromide during the absorption process in the absorptive refrigeration units.
The cooling means may include a plurality of absorptive refrigeration units, each unit being supplied by hot water which has been heated, in use, by hot gases from a fume treatment plant in an aluminium smelting plant; and a chilled water circuit wherein water is circulated through the refrigeration units during which time it is chilled, in use, to a heat exchanger located at a gas turbine air inlet and back to the refrigeration units.
The waste heat produced by the aluminium smelting process may be recovered for absorption cooling from the power production, casting process, the anode baking kilns or the electrolytic reduction cells.
According to a second aspect of the invention, there is provided a process for cooling gas turbine inlet air, including the steps of lowering the temperature of a fluid by means of absorptive refrigeration and using the fluid to cool the gas turbine inlet air.
The chilled water from the absorption coolers may also provide air conditioning comfort cooling for the plant personnel.
According to a third aspect of the invention, there is provided a gas turbine including a cooling arrangement as described in the specification.
According to a fourth aspect of the invention, there is provided an aluminium smelting plant including at least one gas turbine as described herein.
The process may include the step of using waste hot gases to energize the absorptive refrigeration means.
BRIEF DESCRIPTION OF THE DRAWING
One embodiment of the invention will now be described in more detail with reference to the accompanying drawing which is a schematic representation of a cooling arrangement according to the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
In the drawing, a cooling arrangement 10 according to the invention is shown to include an absorption plant 12 including seven absorptive refrigeration units (not shown). In the preferred embodiment, the absorptive refrigeration units are of the Lithium Bromide and water type.
The absorptive refrigeration units are energized by via twenty four heat recovery points 14. In the present invention, the arrangement 10 is installed in an aluminium smelting plant (not shown) and the heat recovery points 14 are located near fume treatment plants (not shown).
At the fume treatment plants hot gases from aluminium smelting cells (not shown) are treated - typically, by removing hydrogen fluoride by dry scrubbing with alumina.
Prior to scrubbing, the hot fumes 16 are ducted to the heat recovery points 14 as shown. At the heat recovery points 14, a water supply and return circuit 18 contains water which absorbs heat from the hot gases at the heat recovery points 14 and which is pumped at approximately 120 degrees Celsius via supply line 18.1 to the absorption plant 12 where the heated water energizes the absorptive refrigeration units (not shown). The water is then returned via return line 18.2 at approximately 90 degrees Celsius to the heat recovery points and the cycle is repeated.
The fumes exiting the heat recovery are cooled from 130 C to around 100 C. The adsorption efficiency of the alumina scrubbing media is consequently enhanced thus hydrogen fluoride recovery is improved in the order of 25%, reducing harmful emissions from the potroom fume treatment plants.
Hot exhaust fumes 17 exit the heat recovery points 14 and are scrubbed before being expelled to atmosphere.
At the absorption plant 12, a chilling water supply and return circuit 20 contains water which is cooled (or chilled) in the absorption plant 12 to about 15 degrees Celsius and which is then pumped via supply line 20.1 to four gas turbine heat exchangers 22. The water is then returned via return line 20.2 at about 25 degrees Celsius to the absorption plant 12 and the cycle is repeated. Hot ambient air 24, which can have a temperature of 50 degrees Celsius or more in very hot climatic conditions, is ducted through the heat exchanges 22 and is cooled down to about 20 degrees Celsius when it exits. The cooled air 26 is then ducted to gas turbines (not shown) as inlet air where the lower inlet air temperature significantly increases efficiency of the turbines in the production of electricity.
A cooling tower arrangement 28 is provided for lowering the temperature of absorption plant cooling water. The cooling water is used to condense the working fluid of the absorption refrigeration units in the normal operation of these units. A cooling water supply and return circuit 30 contains cooling water which pumped via supply line 30.1 to the absorption plant 12 at about 34 degrees Celsius and returned via return line 30.2 at about 43 degrees Celsius and the cycle is repeated.
Applicant has found that in summer in very hot climatic conditions where the ambient temperature reaches 50 degrees Celsius, the efficiency of its gas turbines at its aluminium smelting plant can drop by up to 25%. The optimum temperature for gas turbine inlet air is about 15 degrees Celsius [ISO Standard] and by reducing the inlet air to about 20 degrees Celsius from 50 degrees Celsius ambient temperature, a significant increase in power output, efficiency and performance of the gas turbines is possible.
There are several advantages to the invention as defined when employed in a single site aluminium smelting plant, including the following:
Cooling the gases from the electrolytic reduction cells (not shown) improves the adsorption ability of alumina scrubbing media thus improving hydrogen fluoride recovery. Cooling the gases entering the fume treatment plants from the electrolytic reduction cells allows operators to increase potline amperage without detrimental effect on the fume treatment plants.
Chilled water from the absorption refrigeration process may be used to provide comfort cooling [air conditioning] for plant personnel.
Waste heat for absorption cooling within an aluminium smelter may be recovered from power production, casting process, anode baking kilns, desalination or reduction cells.
Cooling the gases from the electrolytic reduction cells extends filter bag life.
It will be appreciated that many variations or modifications of this invention are possible without departing from the scope of the appended claims.

Claims

1. A cooling arrangement for cooling inlet air for a gas turbine, including cooling means and a heat exchanger located in an air inlet path of the gas turbine.
2. An arrangement as claimed in claim 1 wherein the cooling means is an absorptive refrigeration means.
3. An arrangement as claimed in claim 2 wherein the refrigeration means is a Lithium Bromide and water type absorptive refrigeration means.
4. An arrangement as claimed in claims 2 or 3 wherein the refrigeration means includes a plurality of absorptive refrigeration units, each unit being supplied by hot water which has been heated, in use, by hot gases from a fume treatment plant in an aluminium smelting plant; and a chilled water circuit wherein water is circulated through the refrigeration units during which time it is chilled, in use, to a heat exchanger located at a gas turbine air inlet and back to the refrigeration units.
5. An arrangement as claimed in claim 4 including a cooling water supply and return circuit, via a cooling tower arrangement for purposes of condensing water used during the absorption process in the absorptive refrigeration units.
6. An arrangement as claimed in any one of the previous claims wherein the heat exchanger has chilled water, which has been chilled by the refrigeration means, circulating through it, in use, and through which heat exchanger inlet air for a gas turbine is passed to cool the air down prior to entering the gas turbine.
7. A process for cooling gas turbine inlet air, including the steps of lowering the temperature of a fluid by means of absorptive refrigeration and using the fluid to cool the gas turbine inlet air.
8. A process as claimed in claim 7 including the step of using waste hot gases in an aluminium smelting plant to energize the absorptive refrigeration means.
9. A gas turbine including a cooling arrangement as claimed in any one of claims 1 to 6.
10. An aluminium smelting plant including at least one gas turbine as claimed in claim 9.
PCT/IB2008/000353 2007-03-20 2008-02-18 Cooling arrangement of a gas turbine air inlet WO2009030987A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AE795907 2007-03-20
AE7959/2007 2007-03-20

Publications (2)

Publication Number Publication Date
WO2009030987A2 true WO2009030987A2 (en) 2009-03-12
WO2009030987A3 WO2009030987A3 (en) 2009-05-22

Family

ID=40429449

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2008/000353 WO2009030987A2 (en) 2007-03-20 2008-02-18 Cooling arrangement of a gas turbine air inlet

Country Status (1)

Country Link
WO (1) WO2009030987A2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102765932A (en) * 2012-08-16 2012-11-07 郑州远东耐火材料有限公司 Integrated casting method of electric smelting zirconia alumina charge bars
WO2019057057A1 (en) * 2017-09-20 2019-03-28 University Of Science And Technology Beijing Methods for producing 2024 and 7075 aluminum alloys by recycling waste aircraft aluminum alloys

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5655373A (en) * 1994-09-28 1997-08-12 Kabushiki Kaisha Toshiba Gas turbine intake air cooling apparatus
US6000211A (en) * 1997-06-18 1999-12-14 York Research Corporation Solar power enhanced combustion turbine power plant and methods

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5655373A (en) * 1994-09-28 1997-08-12 Kabushiki Kaisha Toshiba Gas turbine intake air cooling apparatus
US6000211A (en) * 1997-06-18 1999-12-14 York Research Corporation Solar power enhanced combustion turbine power plant and methods

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102765932A (en) * 2012-08-16 2012-11-07 郑州远东耐火材料有限公司 Integrated casting method of electric smelting zirconia alumina charge bars
WO2019057057A1 (en) * 2017-09-20 2019-03-28 University Of Science And Technology Beijing Methods for producing 2024 and 7075 aluminum alloys by recycling waste aircraft aluminum alloys
US11685966B2 (en) 2017-09-20 2023-06-27 The Boeing Company Methods for producing 2024 and 7075 aluminum alloys by recycling waste aircraft aluminum alloys

Also Published As

Publication number Publication date
WO2009030987A3 (en) 2009-05-22

Similar Documents

Publication Publication Date Title
JP6117444B2 (en) Centralized heat supply apparatus and heat supply method for gas-steam combined cycle
EP1336724B1 (en) Exhaust heat utilization method for carbon dioxide recovery process
CN107905897B (en) Gas turbine circulating flue gas waste heat recovery and inlet air cooling combined system and method
CN110145408B (en) Comprehensive energy supply system for recovering wide-concentration gas in coal mine and operation method thereof
CA2822014C (en) Metallurgical plant gas cleaning system, and method of cleaning an effluent gas
CN101435089A (en) System and method for utilizing residual heat of electrolyzer low temperature flue gas
BRPI0515342A (en) method and system for energy recovery and / or cooling in at least one electrolysis cell
Sørhuus et al. Possible use of 25 MW thermal energy recovered from the potgas at Alba line 4
CN208365871U (en) A kind of natural gas smoke waste heat all recovering device
CN203259020U (en) Device generating power by means of sintering kiln tail gas low temperature exhaust heat
WO2009030987A2 (en) Cooling arrangement of a gas turbine air inlet
CN106638783A (en) High-efficiency energy-saving air water production device
RU119393U1 (en) HEAT ELECTRIC POWER STATION WITH ABSORPTION BROWN-LITHIUM REFRIGERATING MACHINE
CN205109079U (en) Gas -liquid separation type air cooler
CN115370428A (en) Multi-energy coupling compressed air energy storage power generation system and operation method
JP2010116855A (en) Gas turbine plant and method for increasing output thereof
CN212408714U (en) Coal-fired power plant waste heat and water recovery system
CN212692569U (en) Dry quenching air cooling condensing system
CN103836987A (en) Flue gas waste heat power-generation energy-conservation and dust-removal method for electric furnace with liquid storage tank
CN104047730A (en) Gas turbine air inlet cooling system by using cascaded lithium bromide refrigerators
CN212777382U (en) Waste incineration power station waste heat utilization system based on absorption heat pump
CN204672102U (en) A kind of regenerating unit of collecting carbonic anhydride
CN112902208A (en) Multi-pollutant integrated removing and cooling system and method utilizing flue gas waste heat
CN103383195A (en) Waste heat utilization and dust removing method for electric furnace flue gas with thermal storage soaking device
CN204923587U (en) Utilize cryogenic cooling tower vapor condensation recovery device of industry low temperature waste heat

Legal Events

Date Code Title Description
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 08709826

Country of ref document: EP

Kind code of ref document: A2