PL426048A1 - Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation - Google Patents

Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation

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Publication number
PL426048A1
PL426048A1 PL426048A PL42604818A PL426048A1 PL 426048 A1 PL426048 A1 PL 426048A1 PL 426048 A PL426048 A PL 426048A PL 42604818 A PL42604818 A PL 42604818A PL 426048 A1 PL426048 A1 PL 426048A1
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PL
Poland
Prior art keywords
gas
exhaust gases
power generating
pressure
bar
Prior art date
Application number
PL426048A
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Polish (pl)
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PL241609B1 (en
Inventor
Leszek Remiorz
Grzegorz Wiciak
Krzysztof Grzywnowicz
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Politechnika Śląska
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.)
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Application filed by Politechnika Śląska filed Critical Politechnika Śląska
Priority to PL426048A priority Critical patent/PL241609B1/en
Publication of PL426048A1 publication Critical patent/PL426048A1/en
Publication of PL241609B1 publication Critical patent/PL241609B1/en

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treating Waste Gases (AREA)

Abstract

Przedmiotem zgłoszenia jest sposób prowadzenia procesu separacji gazów spalinowych zwłaszcza dwutlenku węgla w układach energetycznych zwłaszcza gazowo-parowych, który polega na tym, że dokonuje się co najmniej jednoetapowego osuszenia spalin pochodzących z kotła odzyskowego (1) poprzez ich ochłodzenie do temperatury niższej od temperatury punktu rosy osuszanych spalin w zintegrowanym termoakustycznym urządzeniu chłodniczym (2), następnie podnosi się ich ciśnienie do wartości w zakresie od 1,5 bar do 15 bar w ciśnieniowym wymienniku ciepła (6) zasilanego spalinami o wysokich parametrach, wynoszących co najmniej 450°C oraz 1,05 bar, pochodzącymi korzystnie z ekspandera turbiny gazowej (4), po czym osuszone i podgrzane spaliny o podwyższonym ciśnieniu wynoszącym co najmniej 1,5 bar i podwyższonej temperaturze wynoszącej co najmniej60°C doprowadza się do układu separacji membranowej (8). Przedmiotem zgłoszenia jest też układ do prowadzenia procesu separacji gazów spalinowych zwłaszcza dwutlenku węgla, który charakteryzuje się tym, że składa się z co najmniej jednego zintegrowanego termoakustycznego urządzenia chłodniczego (2) połączonego trwale z silnikiem termoakustycznym (3), deszczownicy (5) i zintegrowanego ciśnieniowego wymiennika ciepła (6), którego integralną część stanowi co najmniej jeden zbiornik ciśnieniowy (7), oraz układu separacji membranowej (8), usytuowanych w ciągu kanału spalinowego (9) układu energetycznego, który połączony jest poprzez orurowanie z wylotem kotła odzyskowego (1) oraz co najmniej jednym wylotem ekspandera turbiny gazowej (4).The subject of the application is the method of conducting the flue gas separation process, especially carbon dioxide in energy systems, especially gas and steam, which consists in the fact that at least one-stage drying of the flue gases from the recovery boiler (1) is carried out by cooling them to a temperature lower than the dew point temperature the exhaust gases are dried in an integrated thermo-acoustic cooling device (2), then their pressure is increased to a value in the range from 1.5 bar to 15 bar in a pressure heat exchanger (6) supplied with high-performance exhaust gases of at least 450 ° C and 1, 05 bar, preferably from the gas turbine expander (4), then the dried and heated exhaust gas with an increased pressure of at least 1.5 bar and an elevated temperature of at least 60 ° C is fed to the membrane separation system (8). The subject of the application is also a system for the separation of exhaust gases, especially carbon dioxide, which is characterized by the fact that it consists of at least one integrated thermo-acoustic cooling device (2) permanently connected with a thermo-acoustic motor (3), a rain shower (5) and an integrated pressure a heat exchanger (6), the integral part of which is at least one pressure vessel (7), and a membrane separation system (8) located in the flue gas duct (9) of the power system, which is connected via piping to the outlet of the recovery boiler (1) and at least one outlet of a gas turbine expander (4).

PL426048A 2018-06-25 2018-06-25 Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation PL241609B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL426048A PL241609B1 (en) 2018-06-25 2018-06-25 Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL426048A PL241609B1 (en) 2018-06-25 2018-06-25 Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation

Publications (2)

Publication Number Publication Date
PL426048A1 true PL426048A1 (en) 2020-01-02
PL241609B1 PL241609B1 (en) 2022-11-07

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PL426048A PL241609B1 (en) 2018-06-25 2018-06-25 Method for running the process of exhaust gases separation in particular of carbon dioxide in power generating systems in particular in gas and steam power generating systems and system for its implementation

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PL241609B1 (en) 2022-11-07

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