PL429009A1 - Heat exchanger fin with thermosiphon effect - Google Patents

Heat exchanger fin with thermosiphon effect

Info

Publication number
PL429009A1
PL429009A1 PL429009A PL42900919A PL429009A1 PL 429009 A1 PL429009 A1 PL 429009A1 PL 429009 A PL429009 A PL 429009A PL 42900919 A PL42900919 A PL 42900919A PL 429009 A1 PL429009 A1 PL 429009A1
Authority
PL
Poland
Prior art keywords
gases
mercury
raw material
heat exchanger
sulfur
Prior art date
Application number
PL429009A
Other languages
Polish (pl)
Other versions
PL240239B1 (en
Inventor
Rafał Andrzejczyk
Tomasz Muszyński
Original Assignee
Politechnika Gdańska
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 Politechnika Gdańska filed Critical Politechnika Gdańska
Priority to PL429009A priority Critical patent/PL240239B1/en
Publication of PL429009A1 publication Critical patent/PL429009A1/en
Publication of PL240239B1 publication Critical patent/PL240239B1/en

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  • Treating Waste Gases (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

Przedmiotem zgłoszenia jest sposób oczyszczania gazów odlotowych z pieców do wypalania klinkieru z tlenków azotu, siarki i rtęci, który charakteryzuje się tym, że w procesie przemiału surowca uzyskuje się odpowiednią wilgotność, temperaturę i stopień zapylenia gazów znajdujących się w układzie wypalania a następnie poprzez reaktor oczyszczania gazów (7) wprowadza się do nich utleniacz w formie mocno zdyspergowanych kropel-mgły ponadto w reaktorze (7) przeprowadzana jest retencja oczyszczanych gazów z wprowadzonym utleniaczem w czasie co najmniej 5 sek a dodatkowe obniżenie emisji rtęci z oczyszczanych gazów uzyskuje się poprzez częściowe lub całkowite usuwanie pyłów z filtrów (8) oraz (10) powstałych po procesie końcowego odpylania i zwracanie ich do układu wypalania jako część mąki surowcowej a w przypadku wyższych stężeń rtęci częściowe lub całkowicie usuwane z układu wypalania poprzez by-pass. Zgłoszenie obejmuje także układ do oczyszczania gazów odlotowych z pieców do wypalania klinkieru z tlenków azotu, siarki i rtęci składający się z pieca (1), cyklonowego wymiennika ciepła (2), wentylatorów (3, 10) młynowni surowca (4), filtrów (9, 11), charakteryzujący się tym, że pomiędzy młynownią surowca (4) a filtrem końcowym (9) wprowadzony jest dodatkowy układ składający się z odpylacza gazów (5), reaktora oczyszczania gazów (7) oraz wentylatora (8).The subject of the application is a method of cleaning flue gases from clinker burning kilns from nitrogen oxides, sulfur and mercury, which is characterized by the fact that in the process of grinding the raw material appropriate humidity, temperature and degree of dusting of gases in the burnout system are obtained, and then through the purification reactor gases (7), an oxidant is introduced into them in the form of highly dispersed mist-drops, moreover, in the reactor (7), the retention of the purified gases with the introduced oxidant is carried out for at least 5 seconds, and an additional reduction of mercury emissions from the purified gases is achieved by partial or complete removing dust from filters (8) and (10) resulting from the final dedusting process and returning them to the firing system as part of the raw flour, and in the case of higher mercury concentrations, partially or completely removed from the firing system by bypass The application also covers a system for cleaning flue gases from clinker kilns from nitrogen oxides, sulfur and mercury consisting of a kiln (1), a cyclone heat exchanger (2), fans (3, 10), raw material mills (4), filters (9 , 11), characterized in that an additional system consisting of a gas dust separator (5), a gas purification reactor (7) and a fan (8) is introduced between the mill of the raw material (4) and the final filter (9).

PL429009A 2019-02-22 2019-02-22 Heat exchanger fin with thermosiphon effect PL240239B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL429009A PL240239B1 (en) 2019-02-22 2019-02-22 Heat exchanger fin with thermosiphon effect

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL429009A PL240239B1 (en) 2019-02-22 2019-02-22 Heat exchanger fin with thermosiphon effect

Publications (2)

Publication Number Publication Date
PL429009A1 true PL429009A1 (en) 2020-08-24
PL240239B1 PL240239B1 (en) 2022-03-07

Family

ID=72143135

Family Applications (1)

Application Number Title Priority Date Filing Date
PL429009A PL240239B1 (en) 2019-02-22 2019-02-22 Heat exchanger fin with thermosiphon effect

Country Status (1)

Country Link
PL (1) PL240239B1 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170051954A1 (en) * 2014-03-24 2017-02-23 The Coca-Cola Company Refrigeration system with phase change material heat exchanger
PL234838B1 (en) * 2017-07-05 2020-04-30 Globimix Spolka Z Ograniczona Odpowiedzialnoscia Accumulator with phase-change bed

Also Published As

Publication number Publication date
PL240239B1 (en) 2022-03-07

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