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A CONCEPT OF THE GASIFICATION PLANT FOR SELECTED ORGANIC WASTE Cover

A CONCEPT OF THE GASIFICATION PLANT FOR SELECTED ORGANIC WASTE

By: Monika CZOP  
Open Access
|Oct 2019

Figures & Tables

Figure 1.

Directions of municipal waste management in Poland [4–6]
Directions of municipal waste management in Poland [4–6]

Figure 2.

Directions of thermal transformation of waste (owe work)
Directions of thermal transformation of waste (owe work)

Figure 3.

Flowchart of the plant for gasification of waste [22]
Flowchart of the plant for gasification of waste [22]

Figure 4.

Tested waste: (a) waste plastic (WP); (b) initially prepared municipal waste (MW) (performed by M. Czop)
Tested waste: (a) waste plastic (WP); (b) initially prepared municipal waste (MW) (performed by M. Czop)

Technical parameters of the plant for gasification of waste [22]

The type of depositCirculating fluidized bed
Process temperature, °C1200
Working pressure, MPa1.0–1.5
Reactor operating pressure, MPa2.0
Gasification agentsteam/ O2/ CO2

Standards for the physicochemical analysis

TitleUnitSymbolStandard
Determination of moisture content%MTPN-Z-15008-02:1993
Determining combustion heat and calculating the calorific valueMJ/kgGCV, NCVPN-Z-15008-04:1993
Determination of ash content%APN-EN 15403:2011
Determination of fly ash by weighting%VPN-EN 15402:2011
Determination of carbon and hydrogen%C, HPN-Z-15008-05:1993
Determination of nitrogen with the Kjeldahl method%NPN-G-04523:1992
Determination of sulfur with the Eschka method%SPN-ISO 334:1997
Determination of chloride using the Eschka mixture%ClPN-ISO 587:2000

The composition of synthesis gas from the process for WP

ComponentsSymbolUnitThe composition of synthesis gas for WP
HydrogenH2 vol %51.64
Carbon monoxideCO46.10
NitrogenN2 0.44
SteamH2O0.78
Carbon dioxideCO2 0.27
ArgonAr0.67
Sulfur dioxideSO2 0.00
Hydrogen sulfideH2Sppm429
AmmoniaNH3 ppm20
Hydrogen chlorideHClppm349
Gross calorific valueGCVMJ/kg19.03
Net calorific valueNCVMJ/kg17.44

The composition of synthesis gas from the process for MW

ComponentsSymbolUnitThe composition of synthesis gas for WP
HydrogenH2 vol %43.98
Carbon monoxideCO46.74
NitrogenN2 0.59
SteamH2O5.81
Carbon dioxideCO2 2.43
Sulfur dioxideSO2 0.00
Hydrogen sulfideH2Sppm2500
AmmoniaNH3 ppm23
Hydrogen chlorideHClppm988
Gross calorific valueGCVMJ/kg15.85
Net calorific valueNCVMJ/kg14.49

Technical analysis of tested raw materials for the gasification process

ParameterSymbolUnitWPMW
Total moisture contentMT%0.0322.47
Combustible substances, Air DriedXd %99.1092.44
Combustible substances, As ReceivedXar %99.0771.67
Ash, Air DriedAd %0.867.56
Ash, As ReceivedAar %0.865.86
Volatile matter, Air DriedVd %99.1379.06
Gross calorific value, Air DriedGCVd MJ/kg47.5223.66
Gross calorific value, As ReceivedGCVar 47.5018.29
Net calorific value, Air DriedNCVd MJ/kg44.3822.62
Net calorific value, As ReceivedNCVar 44.3616.97

Elemental composition of selected waste

ParameterSymbolUnitWPMW
AsReceivedAirDriedAsReceivedAirDried
CarbonC%85.2885.3134.6343.29
HydrogenH%13.9513.963.424.27
SulphurS%0.220.220.470.59
NitrogenN%0.290.290.881.10
ChlorineCl%0.190.190.410.51
OxygenO%0.000.0031.8639.64
DOI: https://doi.org/10.21307/acee-2019-042 | Journal eISSN: 2720-6947 | Journal ISSN: 1899-0142
Language: English
Page range: 123 - 129
Submitted on: Jun 18, 2019
Accepted on: Jun 24, 2019
Published on: Oct 18, 2019
Published by: Silesian University of Technology
In partnership with: Paradigm Publishing Services
Publication frequency: 4 issues per year

© 2019 Monika CZOP, published by Silesian University of Technology
This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 License.