PL424069A1 - Method for conducting the process of thermolysis of multi-component wastes - Google Patents
Method for conducting the process of thermolysis of multi-component wastesInfo
- Publication number
- PL424069A1 PL424069A1 PL424069A PL42406917A PL424069A1 PL 424069 A1 PL424069 A1 PL 424069A1 PL 424069 A PL424069 A PL 424069A PL 42406917 A PL42406917 A PL 42406917A PL 424069 A1 PL424069 A1 PL 424069A1
- Authority
- PL
- Poland
- Prior art keywords
- gas
- thermolysis
- subject
- subjected
- hydrocarbons
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 9
- 238000001149 thermolysis Methods 0.000 title abstract 4
- 239000002699 waste material Substances 0.000 title abstract 3
- 229930195733 hydrocarbon Natural products 0.000 abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 abstract 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract 2
- 229910052782 aluminium Inorganic materials 0.000 abstract 2
- 239000004743 Polypropylene Substances 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000004821 distillation Methods 0.000 abstract 1
- 239000011888 foil Substances 0.000 abstract 1
- 238000000227 grinding Methods 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000007791 liquid phase Substances 0.000 abstract 1
- 239000012528 membrane Substances 0.000 abstract 1
- -1 polypropylene Polymers 0.000 abstract 1
- 229920001155 polypropylene Polymers 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
Przedmiotem zgłoszenia jest sposób prowadzenia procesu termolizy odpadów wieloskładnikowych w warunkach beztlenowych, charakteryzujący się tym, że odpady wieloskładnikowe poddawane są rozdrobnieniu do frakcji o wielkości od 20 mm x 20 mm do frakcji 20 mm x 150 mm a następnie podawane są do przeponowo podgrzewanego, poziomego, reaktora obrotowego, w którym prowadzona jest termoliza w temperaturze od 200°C do 350°C pod ciśnieniem od 0,1 MPa do 0,25 MPa, przez ok 2,5 godzin następnie w temperaturze 350°C przez kolejną 1 godzinę, następnie gaz procesowy poddawany jest kondensacji w dalszej części układu, w temperaturze gazu wchodzącego na skraplacze, która wynosi co najmniej 250°C do 350°C, gdzie następuje wydzielanie węglowodorów pochodzące z termolizy papieru i polipropylenu węglowodory nie skroplone w skraplaczach wędrują na filtr gazowy i zbiorniki gazowe, a następnie wędrują na palniki gazowe zasilając układ reaktora, przy czym w trakcie procesu odzyskuje się aluminium, które wydzielane jest w postaci folii aluminiowej i dalej poddawane jest procesowi oczyszczania; natomiast węglowodory płynne w postaci trzech faz ciekłych: lekkiej, średniej i ciężkiej poddawane są destylacji, w wyniku której uzyskuje się frakcje zawierające wydzielone węglowodory; pozostały gaz poprocesowy poddawany jest skropleniu i oczyszczeniu podawany jest na palniki do ogrzewania reaktora. Przedmiotem zgłoszenia jest również układ do realizacji tego sposobu. Przedmiotem zgłoszenia jest też układ, w którym przebiega proces według przedmiotowego sposobu.The subject of the application is a method of thermolysis of multi-component waste under anaerobic conditions, characterized in that the multi-component waste is subjected to grinding to the fraction size from 20 mm x 20 mm to the 20 mm x 150 mm fraction and then fed to the membrane, horizontal, rotary reactor in which thermolysis is carried out at a temperature from 200 ° C to 350 ° C at a pressure from 0.1 MPa to 0.25 MPa, for about 2.5 hours then at 350 ° C for another 1 hour, then gas the process is subjected to condensation in the further part of the system, at a temperature of gas entering the condensers, which is at least 250 ° C to 350 ° C, where hydrocarbons are released from the thermolysis of paper and polypropylene, non-condensed hydrocarbons in the condensers go to the gas filter and gas tanks and then they travel to gas burners feeding the reactor system during the process aluminum is recovered, which is separated in the form of aluminum foil and is further subjected to a purification process; while liquid hydrocarbons in the form of three liquid phases: light, medium and heavy are subjected to distillation, which produces fractions containing separated hydrocarbons; the remaining post-process gas is liquefied and cleaned and fed to the reactor heating burners. The subject of the notification is also a system for implementing this method. The subject of the application is also a system in which the process according to the subject method is carried out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL424069A PL237735B1 (en) | 2017-12-28 | 2017-12-28 | Method for conducting the process of thermolysis of multi-component wastes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL424069A PL237735B1 (en) | 2017-12-28 | 2017-12-28 | Method for conducting the process of thermolysis of multi-component wastes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL424069A1 true PL424069A1 (en) | 2019-07-01 |
| PL237735B1 PL237735B1 (en) | 2021-05-17 |
Family
ID=67105529
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL424069A PL237735B1 (en) | 2017-12-28 | 2017-12-28 | Method for conducting the process of thermolysis of multi-component wastes |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL237735B1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2600530A1 (en) * | 1975-02-10 | 1976-08-19 | Deco Ind | PROCESS AND EQUIPMENT FOR OBTAINING USABLE HYDROCARBON PRODUCTS |
| PL209828B1 (en) * | 2007-11-30 | 2011-10-31 | Przedsiębiorstwo Ekonaks Społka Z Ograniczoną Odpowiedzialnością | Processing method of plastic wastes, especially polyphenoles and device for processing method of plastic wastes, especially polyphenoles |
| PL210734B1 (en) * | 2006-10-02 | 2012-02-29 | Zbigniew Pabian | Dynamic distillating machine |
| PL221831B1 (en) * | 2012-06-21 | 2016-06-30 | Jodkowski Wiesław Helioterm | Method for processing plastic waste, especially polyolefin, and a device for processing plastic waste, especially polyolefin |
-
2017
- 2017-12-28 PL PL424069A patent/PL237735B1/en unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2600530A1 (en) * | 1975-02-10 | 1976-08-19 | Deco Ind | PROCESS AND EQUIPMENT FOR OBTAINING USABLE HYDROCARBON PRODUCTS |
| PL210734B1 (en) * | 2006-10-02 | 2012-02-29 | Zbigniew Pabian | Dynamic distillating machine |
| PL209828B1 (en) * | 2007-11-30 | 2011-10-31 | Przedsiębiorstwo Ekonaks Społka Z Ograniczoną Odpowiedzialnością | Processing method of plastic wastes, especially polyphenoles and device for processing method of plastic wastes, especially polyphenoles |
| PL221831B1 (en) * | 2012-06-21 | 2016-06-30 | Jodkowski Wiesław Helioterm | Method for processing plastic waste, especially polyolefin, and a device for processing plastic waste, especially polyolefin |
Also Published As
| Publication number | Publication date |
|---|---|
| PL237735B1 (en) | 2021-05-17 |
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