🇵🇱 INSTYTUT TECHNOLOGII PALIW I ENERGII PL
石油化工与燃料环境水与废水
INSTYTUT TECHNOLOGII PALIW I ENERGII 是由 PCA 认可的实验室，认可编号 AB 081（Zabrze，波兰）。认可范围涵盖 386 项检测方法，涉及以下领域：石油化工与燃料、环境、水与废水。检测对象包括：民用固体燃料燃烧器具 — 嵌入式器具，含明火式、民用固体燃料燃烧器具 — 房间加热器、民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料、颗粒燃料房间加热器。
要点速览
- 认可编号: PCA AB 081
- 认可范围内方法数: 386
- 检测对象种类: 32
- 城市: Zabrze, 波兰
- 认可编号
- AB 081
- 认可机构
- PCA
- 地址
- ul. Zamkowa 1, 41-803 Zabrze
- 城市
- Zabrze, 波兰
该实验室检测什么 (32)
- 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 — 32 项方法
- 民用固体燃料燃烧器具 — 房间加热器 — 32 项方法
- 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 — 32 项方法
- 颗粒燃料房间加热器 — 32 项方法
- 固体燃料嵌入式器具，含明火式壁炉 — 31 项方法
- 固体燃料房间加热器 — 31 项方法
- 民用固体燃料燃烧器具 — 31 项方法
- 固体燃料供暖锅炉 — 24 项方法
- Solid fuels: - solid biomass - solid biofuels — 22 项方法
- Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 — 17 项方法
- Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels — 14 项方法
- Activated carbons — 10 项方法
- Furnace waste, code: ex 20 01 99 (ashes from households) — 9 项方法
- Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 — 8 项方法
- Liquid fuel fireplaces — 8 项方法
- 另有 17 项
认可范围 — 项检测方法 (386)
| 序号 | 检测对象 | 方法 / 参数 | 技术 | 依据文件 | |
|---|---|---|---|---|---|
| 检测方法 | |||||
| 1 | Gaseous fuels: - coke oven gas | Content of gaseous components Range: hydrogen (53,00 – 65) % v/v oxygen (0,20 – 2) % v/v nitrogen (1,50 – 10) % v/v carbon monoxide (4,50 – 9) % v/v carbon dioxide (1,50 – 4) % v/v methane (18,00 – 28) % v/v ethane (0,10 – 1,50) % v/v ethylene (1,00 – 4) % v/v propane (0,01 – 0,20) % v/v propylene (0,05 – 0,25) % v/v n-butane (0,01 – 0,10) % v/v Gas chromatography with flame ionization and thermal conductivity detection (GC-FID, GC-TCD) method | PN-93/C-96012 Metoda C | ||
| 2 | Gaseous fuels: - coke oven gas | Gross calorific value, net calorific value, density based on the composition (calculated) | PN-EN ISO 6976:2016-11 | ||
| 3 | Solid fuels: - brown coal | Total moisture content Range: (1,0 – 70,0) % Gravimetric method | PN-G-04511:1980 pkt. 2.3.2 | ||
| 4 | Solid fuels: - hard coal - coke from hard coal Processed solid fuels | Total moisture content Range: (0,1 – 60,0) % Gravimetric method | PN-G-04611:2020-06 | ||
| 5 | Solid fuels: - hard coal - coke from hard coal Processed solid fuels | Moisture content in the analytical sample Range: (0,1 – 18,0) % Gravimetric method | |||
| 6 | 固体燃料： — 烟煤 | Transient moisture content Range: (1,0 – 60,0) % Gravimetric method | |||
| 7 | Solid fuels: - brown coal | Transient moisture content Range: (2,5 – 60,0) % Gravimetric method | PN-80/G-04511 | ||
| 8 | Solid fuels: - brown coal | Moisture content in the analytical sample Range: (5,0 – 18,0) % Gravimetric method | |||
| 9 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Ash content Range: (0,1 – 50,0) % Gravimetric method | PN-80/G-04512+Az1:2002 PN-ISO 1171:2002 | ||
| 10 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Volatile matter content Range: (0,10 – 50,00) % Gravimetric method | PN-G-04516:1998 ISO 562:2024-08 | ||
| 11 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Moisture content in the analytical sample Range: (0,1 – 18,0) % Thermogravimetric method (TGA) | PN-G-04560:1998 | ||
| 12 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Ash content Range: (0,1 – 50,0) % Thermogravimetric method (TGA) | |||
| 13 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Gross calorific value Range: (5000 – 40 000) kJ/kg Calorimetric method | PN-81/G-04513 PN-ISO 1928:2020-05 | ||
| 14 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | 低位发热量（计算值） | |||
| 15 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | CO 2 emission factor (calculated) | Procedura Q/LCA/60/B:2022 | ||
| 16 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Content of total sulphur and sulphur in ash Range: (0,01 – 8,00) % High-temperature combustion method with IR detection | PN-G-04584:2001 | ||
| 17 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Content of ash and combustible sulphur (calculated) | |||
| 18 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Total sulphur content Range: (0,01 – 4,00) % High-temperature combustion method with IR detection | ISO 19579:2006 | ||
| 19 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Content of carbon and hydrogen Range: carbon (20,0 – 100) % hydrogen (0,01 – 8,00) % High-temperature combustion method with IR detection | PN-G-04571:1998 ISO 29541:2025-02 | ||
| 20 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Nitrogen content Range: (0,05 – 2,00) % High-temperature combustion method with TC detection | |||
| 21 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Chlorine content Range: (0,009 – 1,500) % Potentiometric titration method | PN-G-04534:2024-01 | ||
| 22 | Solid fuels: - hard coal - lignite - coke from hard coal Processed solid fuels | Characteristic fusibility temperatures of ash Range: (815 – 1650) oC High-temperature method with image observation | PN-ISO 540:2001 (ISO 540:1995 IDT) | ||
| 23 | Solid fuels: - hard coal - brown coal - coke from hard coal | Content of elements in ash expressed as oxides Range: SiO (0,46 – 62,00) % 2 Al O (0,16 – 33,00) % 2 3 Fe O (0,03 – 20,00) % 2 3 CaO (0,36 – 36,00) % MgO (0,09 – 11,00) % Na O (0,05 – 6,50) % 2 K O (0,03 – 3,00) % 2 P O (0,01 – 2,90) % 2 5 SO (0,08 – 18,90) % 3 Mn O (0,01 – 1,70) % 3 4 TiO (0,01 – 2,50) % 2 BaO (0,01 – 1,40) % SrO (0,01 – 1,50) % Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/55/B:2022 | ||
| 24 | Solid fuels: - hard coal - brown coal - coke from hard coal | Content of elements in fuel (calculated) | |||
| 25 | 固体燃料： — 烟煤 | Moisture content in the analytical sample Range: (0,01 – 18,0) % Gravimetric method | PN-ISO 11722:2009 | ||
| 26 | 固体燃料： — 烟煤 | Total moisture content Range: (0,01 – 60,0) % Gravimetric method | PN-ISO 589:2006 Metoda B1 | ||
| 27 | 固体燃料： — 烟煤 | Content of fraction with grain size 3,0 – 40,0 mm Range: (0,0 – 100) % Gravimetric method | ISO 1953:2015 pkt. 6.2 | ||
| 28 | 固体燃料： — 烟煤 | Caking power Range: (0 – 90) Roga method | PN-G-04508:2020-05 | ||
| 29 | 固体燃料： — 烟煤 | Dilatometric indices Range: a = (10 – 40) % b = (none – 200) % Audibert-Arnu method | PN-81/G-04517 ISO 349:2020 | ||
| 30 | Solid fuels: - brown coal | Total moisture content Range: (5,0 – 60,0) % Gravimetric method | ISO 5068-1:2007 | ||
| 31 | Solid fuels: - brown coal | Moisture content in the analytical sample Range: (2,0 – 23,0) % Gravimetric method | ISO 5068-2:2007 | ||
| 32 | Solid fuels: - hard coal - brown coal | Fluorine content Range: (0,005 – 0,050) % Potentiometric method | PN-82/G-04543 | ||
| 33 | Solid fuels: - hard coal - brown coal | Mercury content Range: (0,010 – 1,000) mg/kg Cold mercury vapour atomic absorption spectrometry (CVAAS) method | Procedura Q/LCA/32/B:2022 | ||
| 34 | Solid fuels: - hard coal - brown coal | Content of trace elements arsenic (0,68– 500) mg/kg cadmium (0,044 – 500) mg/kg cobalt (0,35 – 500) mg/kg chromium (0,18 – 500) mg/kg copper (0,58 – 500) mg/kg manganese (0,074 – 500) mg/kg molybdenum (0,18 – 500) mg/kg nickel (0,39 – 500) mg/kg lead (1,16 – 500) mg/kg antimony (0,86 – 500) mg/kg vanadium (0,60 – 500) mg/kg zinc (0,10 – 500) mg/kg Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/57/B:2022 | ||
| 35 | Solid fuels: - coke | Moisture content in the analytical sample Range: (0,1 – 5,0) % Gravimetric method | PN-ISO 687:2005 | ||
| 36 | Solid fuels: - coke | Total moisture content Range: (0,1 – 21,0) % Gravimetric method | PN-ISO 579:2002 | ||
| 37 | Solid fuels: - coke | Content of trace elements arsenic (0,40 – 500) mg/kg cadmium (0,13 – 500) mg/kg cobalt (0,48 – 500) mg/kg chromium (0,71– 500) mg/kg copper (1,2 – 500) mg/kg manganese (0,33 – 500) mg/kg molybdenum (0,22 – 500) mg/kg nickel (0,42– 500) mg/kg lead (1,7 – 500) mg/kg antimony (1,1 – 500) mg/kg vanadium (0,35 – 500) mg/kg zinc (1,9 – 500) mg/kg Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/57/B:2022 | ||
| 38 | Solid fuels: - solid biomass - solid biofuels | Gross calorific value Range: (9 000 – 29 000) kJ/kg Calorimetric method | Procedura Q/LCA/12/B:2022 PN-EN ISO 18125:2017-07 | ||
| 39 | Solid fuels: - solid biomass - solid biofuels | 低位发热量（计算值） | |||
| 40 | Solid fuels: - solid biomass - solid biofuels | Total moisture content Range: (0,4 – 80,0) % Gravimetric method | PN-EN ISO 18134-2:2017-03 PN-EN ISO 18134-1:2023-02 | ||
| 41 | Solid fuels: - solid biomass - solid biofuels | Moisture content in the analytical sample Range: (0,4 – 15,0) % Gravimetric method | Procedura Q/LCA/05/B:2022 PN-EN ISO 18134-3:2023-12 | ||
| 42 | Solid fuels: - solid biomass - solid biofuels | Ash content Range: (0,1 – 40,0) % Gravimetric method | Procedura Q/LCA/06/B:2022 PN-EN ISO 18122:2023-05 | ||
| 43 | Solid fuels: - solid biomass - solid biofuels | Volatile matter content Range: (50,00 – 85,00) % Gravimetric method | Procedura Q/LCA/07/B:2022 PN-EN ISO 18123:2023-10 | ||
| 44 | Solid fuels: - solid biomass - solid biofuels | Moisture content in the analytical sample Range: (0,4 – 15,0) % Thermogravimetric method (TGA) | Procedura Q/LCA/27/B:2022 PN-EN ISO 18134-3:2023-12 | ||
| 45 | Solid fuels: - solid biomass - solid biofuels | Ash content Range: (0,1 – 40,0) % Thermogravimetric method (TGA) | Procedura Q/LCA/27/B:2022 PN-EN ISO 18122:2023-05 | ||
| 46 | Solid fuels: - solid biomass - solid biofuels | Total sulphur content Range: (0,02 – 3,00) % High-temperature combustion method with IR detection | Procedura Q/LCA/08/B:2022 | ||
| 47 | Solid fuels: - solid biomass - solid biofuels | Total sulfur content Range: (0,02 – 0,50) % High-temperature combustion method with IR detection | PN-EN ISO 16994:2016-10 | ||
| 48 | Solid fuels: - solid biomass - solid biofuels | Content of carbon and hydrogen Range: carbon (20,0 – 60,0) % hydrogen (2,50 – 8,00) % High-temperature combustion method with IR detection | Procedura Q/LCA/09/B:2022 PN-EN ISO 16948:2015-07 | ||
| 49 | Solid fuels: - solid biomass - solid biofuels | Nitrogen content Range: (0,05 – 10,00) % High-temperature combustion method with TC detection | |||
| 50 | Solid fuels: - solid biomass - solid biofuels | Ash sulphur content Range: (0,02 – 7,00) % High-temperature combustion method with IR detection | Procedura Q/LCA/10/B:2022 | ||
| 51 | Solid fuels: - solid biomass - solid biofuels | Combustible sulfur content (calculated) | |||
| 52 | Solid fuels: - solid biomass - solid biofuels | Chlorine content Range: (0,009 – 2,500) % Potentiometric titration method | Procedura Q/LCA/26/B:2022 | ||
| 53 | Solid fuels: - solid biomass - solid biofuels | Characteristic fusibility temperatures of ash Range: (550 – 1650) oC High-temperature method with image observation | EN ISO 21404:2020-08 | ||
| 54 | Solid fuels: - solid biomass - solid biofuels | Biomass content – mass fraction Range: (70,0 – 99,9) % Non-biomass content – mass fraction Range: (0,1 – 20,0) % Gravimetric method | PN-EN ISO 21644:2021-07 pkt. B7 | ||
| 55 | Solid fuels: - solid biomass - solid biofuels | Mercury content Range: (0,004 – 0,023) mg/kg Cold mercury vapour atomic absorption spectrometry (CVAAS) method | Procedura Q/LCA/53/B:2022 | ||
| 56 | Solid fuels: - solid biomass - solid biofuels | Mechanical strength Range: (75,0 – 99,5) % Gravimetric method | PN-EN ISO 17831-1:2016-02 | ||
| 57 | Solid fuels: - solid biomass - solid biofuels | Content of elements in ash expressed as oxides Range: SiO (0,46 – 81,00) % 2 Al O (0,16 – 5,00) % 2 3 Fe O (0,03 – 5,50) % 2 3 CaO (0,36 – 46,60) % MgO (0,09 – 12,30) % Na O (0,05 – 5,10) % 2 K O (0,03 – 45,70) % 2 P O (0,01 – 41,60) % 2 5 SO (0,08 – 8,20) % 3 Mn O (0,01 – 2,30) % 3 4 TiO (0,01 – 0,24) % 2 BaO (0,01 – 0,26) % SrO (0,01 – 0,20) % Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/56/B:2022 | ||
| 58 | Solid fuels: - solid biomass - solid biofuels | Content of elements in biomass (calculated) | |||
| 59 | Solid fuels: - solid biomass - solid biofuels | Content of trace elements Range: arsenic (0,67 – 170) mg/kg cadmium (0,028 – 170) mg/kg cobalt (0,058 – 170) mg/kg chromium (0,087 – 170) mg/kg copper (0,23 – 170) mg/kg manganese (0,67 – 170) mg/kg molybdenum (0,17 – 170) mg/kg nickel (0,18 – 170) mg/kg lead (1,7 – 170) mg/kg vanadium (0,11 – 170) mg/kg zinc (4,5 – 170) mg/kg antimony (0,39 – 170) mg/kg Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/58/B:2022 | ||
| 60 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Total moisture content Range: (0,4 – 80,0) % Gravimetric method | EN/TS 15414-1:2010 | ||
| 61 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Moisture content in the analytical sample Range: (0,4 – 15,0) % Gravimetric method | PN-EN ISO 21660-3:2021-08 | ||
| 62 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Ash content Range: (0,1 – 60,0) % Gravimetric method | PN-EN ISO 21656:2021-08 | ||
| 63 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Volatile matter content Range: (50,00 – 90,00) % Gravimetric method | PN-EN ISO 22167:2021-08 | ||
| 64 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Total sulphur content Range: (0,01 – 8,00) % High-temperature combustion method with IR detection | PN-EN 15408:2011 | ||
| 65 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Content of carbon and hydrogen Range: carbon (10,0 – 70,0) % hydrogen (1,50 – 10,00) % High-temperature combustion method with IR detection | PN-EN ISO 21663:2021-06 | ||
| 66 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Nitrogen content Range: (0,05 – 10,00) % High-temperature combustion method with TC detection | |||
| 67 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Gross calorific value Range: (5 000 – 40 000) kJ/kg Calorimetric method | PN-EN ISO 21654-2021-12 | ||
| 68 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | 低位发热量（计算值） | |||
| 69 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Chlorine content Range: (0,009 – 7,200) % Potentiometric titration method | Procedura Q/LCA/24/B:2022 | ||
| 70 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Ash content Range: (0,1 – 60,0) % Thermogravimetric method (TGA) | PN-EN ISO 21656:2021-08 | ||
| 71 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Moisture content in the analytical sample Range: (0,4 – 16,0) % Thermogravimetric method (TGA) | PN-EN ISO 21660-3:2021-08 | ||
| 72 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Characteristic fusibility temperatures of ash Range: (550 – 1650) 0C High-temperature method with image observation | EN/TR 15404:2010 | ||
| 73 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Biomass content – mass fraction Range: (10,0 – 99,9) % Non-biomass content – mass fraction Range: (0,1 – 90,0) % Gravimetric method | PN-EN ISO 21644:2021-07 pkt. B7 | ||
| 74 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Content of elements in ash expressed as oxides Range: SiO2 (0,46 – 55,20) % Al2O3 (0,16 – 47,60) % Fe2O3 (0,03 – 46,60) % CaO (0,36 – 17,50) % MgO (0,09 – 20,70) % Na2O (0,05 – 16,90) % K2O (0,03 – 15,00) % P2O5 (0,01 – 30,70) % SO3 (0,08 – 34,10) % Mn3O4 (0,01 – 1,70) % TiO2 (0,01 – 2,20) % BaO (0,01 – 1,40) % SrO (0,05 – 1,50) % Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/65/B:2022 | ||
| 75 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Content of elements in solid recovered fuels, waste (calculated) | |||
| 76 | Solid fuels: - solid recovered fuels Waste, code: O) 02 01 01, 02 01 03, 02 01 04, 02 01 07, 02 01 83, 02 02 04, 02 03 80, 02 03 81, 02 04 80, 02 05 02, 02 06 03, 02 07 05, 02 07 80, 03 01 01, 03 01 05, 03 01 82, 03 03 02, 03 03 07, 03 03 08, 03 03 11, 04 02 09, 04 02 20, 04 02 21, 04 02 22, 07 02 12, 07 02 13, 07 02 80, 15 01 01, 15 01 02, 15 01 03, 15 01 05, 15 01 06, 15 01 09, 16 01 03, 16 01 19, 17 02 01, 17 02 03, 19 08 05, 19 08 12, 19 12 01, 19 12 04, 19 12 08, 19 12 10, 20 01 01, 20 01 10, 20 01 11, 20 01 38, 20 01 39, 20 03 01 | Mercury content Range: (0,015 – 4,50) mg/kg Cold mercury vapour atomic absorption spectrometry (CVAAS) method | Procedura Q/LCA/54/B:2022 | ||
| 77 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Total carbon content Range: (0,1 – 50,0) % High-temperature combustion method with IR detection | Procedura Q/LCA/16/B:2022 | ||
| 78 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Moisture content in the analytical sample Range: (0,1 – 10,0) % Gravimetric method | PN-G-04611:2020-06 pkt. 4.3.2 | ||
| 79 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Moisture content in the analytical sample Range: (0,1 – 10,0) % Thermogravimetric method (TGA) | PN-G-04560:1998 | ||
| 80 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Mercury content Range: (0,005 – 1,000) mg/kg Cold mercury vapour atomic absorption spectrometry (CVAAS) method | Procedura Q/LCA/33/B:2022 | ||
| 81 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Content of elements in the residue after ignition expressed as oxides Range: SiO (0,46 – 89,00) % 2 Al O (0,16 – 47,50) % 2 3 Fe O (0,03 – 33,00) % 2 3 CaO (0,36 – 40,00) % MgO (0,09 – 20,70) % Na O (0,05 – 16,90) % 2 K O (0,03 – 18,00) % 2 P O (0,01 – 5,00) % 2 5 SO (0,08 – 10,00) % 3 Mn O (0,01 – 1,70) % 3 4 TiO (0,01 – 16,50) % 2 BaO (0,01 – 1,40) % SrO (0,01 – 1,50) % Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/62/B:2022 | ||
| 82 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Content of elements in combustion waste (calculated) | |||
| 83 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Content of trace elements arsenic (1,7 – 1000) mg/kg cadmium (0,27 – 1000) mg/kg cobalt (0,14 – 1000) mg/kg chromium (0,74 – 1000) mg/kg copper (0,54 – 1000) mg/kg manganese (3,2 – 1000) mg/kg molybdenum (0,98 – 1000) mg/kg nickel (2,7 – 1000) mg/kg lead (5,4 – 1000) mg/kg antimony (2,0– 1000) mg/kg vanadium (0,64 – 1000) mg/kg zinc (1,0 – 1000) mg/kg Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/63/B:2022 | ||
| 84 | Furnace waste, code: O) 10 01 01, 10 01 02, 10 01 03, 10 01 05, 10 01 07, 10 01 15, 10 01 17, 10 01 23, 10 01 80, 10 01 81, 10 01 82, 10 01 99 19 01 12, 19 01 14, 19 01 16, 19 01 19, 19 01 99 | Loss on ignition Range: (1,5 – 80,0) % Gravimetric method | Procedura Q/LCA/44/B:2022 | ||
| 85 | Furnace waste, code: ex 20 01 99 (ashes from households) | Loss on ignition Range: (3,0 – 90,0) % Gravimetric method | Procedura Q/LCA/44/B:2022 | ||
| 86 | Furnace waste, code: ex 20 01 99 (ashes from households) | Moisture content in the analytical sample Range: (0,1 – 5,0) % Gravimetric method | PN-G-04611:2020-06 pkt. 4.3.2 | ||
| 87 | Furnace waste, code: ex 20 01 99 (ashes from households) | Moisture content in the analytical sample Range: (0,10 – 5,00) % Thermogravimetric method (TGA) | PN-G-04560:1998 | ||
| 88 | Furnace waste, code: ex 20 01 99 (ashes from households) | Total moisture content Range: (0,1 – 18,0) % Gravimetric method | PN-G-04611:2020-06 pkt.4.4.5 | ||
| 89 | Furnace waste, code: ex 20 01 99 (ashes from households) | Ash content Range: (35,0 – 90,0) % Gravimetric method | PN-G-04512:1980/Az1:2002 | ||
| 90 | Furnace waste, code: ex 20 01 99 (ashes from households) | Ash content Range: (35,00 – 90,00) % Thermogravimetric method (TGA) | PN-G-04560:1998 | ||
| 91 | Furnace waste, code: ex 20 01 99 (ashes from households) | Content of elements expressed as oxides in the residue after ignition Range: SiO (4,00 – 60,00) % 2 Al O (1,30 – 35,00) % 2 3 Fe O (0,30 – 45,00) % 2 3 CaO (3,60 – 55,00) % MgO (1,00 – 20,70) % Na O (0,05 – 16,90) % 2 K O (0,30 – 20,00) % 2 P O (0,10 – 27,00) % 2 5 SO (0,08 – 10,00) % 3 Mn O (0,01 – 5,10) % 3 4 TiO (0,01 – 27,00) % 2 BaO (0,10 – 1,50) % SrO (0,05 – 1,00) % Inductively coupled plasma atomic emission spectrometry (ICP-OES) method | Procedura Q/LCA/62/B:2022 | ||
| 92 | Furnace waste, code: ex 20 01 99 (ashes from households) | Element content in waste (calculated) | |||
| 93 | Mechanical and automatic devices for sampling hard coal | Accuracy of sampling, sample preparation and analysis | PN-G-04502:2014-11 pkt.10 | PN-ISO 13909-7:2005 | ||
| 94 | Mechanical and automatic devices for sampling hard coal | Load on the sampling system | PN-ISO 13909-8:2005 | ||
| 95 | Mechanical and automatic devices for sampling solid biomass | Accuracy of sampling, sample preparation and analysis | PN-EN ISO 18135:2017-06 pkt 8 | ||
| 96 | Mechanical and automatic devices for sampling solid biomass | Load on the sampling system | PN-ISO 13909-8:2005 | ||
| 97 | Activated carbons | Fraction content Range: (0,0 – 100) % Gravimetric method | PN-88/C-97555/01 | ||
| 98 | Activated carbons | Methylene number Range: (1 – 50) cm3 Visual method | PN-82/C-97555/03 | ||
| 99 | Activated carbons | Iodine adsorption number Range: (10 – 1450) mg/g Titrimetric method | PN-83/C-97555/04 | ||
| 100 | Activated carbons | Ash content Range: (0,1 – 30) % Gravimetric method | PN-84/C-97555/08 | ||
| 101 | Activated carbons | Water content Range: (0,1 – 40) % Gravimetric method | PN-84/C-97555/09 | ||
| 102 | Activated carbons | Mechanical strength Range: (0,1 – 99,9) % Gravimetric method | PN-90/C-97554 pkt. 5.4.5. PN-EN 12915-1:2009 p.8.2.4 | ||
| 103 | Activated carbons | Bulk density Range: (100 – 1000) g/dcm3 Gravimetric method | PN-90/C-97554 pkt. 5.4.2. PN-EN 12915-1:2009 p. 8.2.3 | ||
| 104 | Activated carbons | Ash content Range: (0,1 – 30) % Gravimetric method | PN-EN 12902:2005 pkt. 6.2 | ||
| 105 | Activated carbons | Water content Range: (0,1 – 40) % Gravimetric method | PN-EN 12902:2005 pkt. 6.5 | ||
| 106 | Activated carbons | Iodine number Range: (600 – 1450) mg/g Titrimetric method | PN-EN 12902:2005 pkt. 6.10 | ||
| 107 | Solid fuels: - hard coal - lignite - coke | 化学与物理检测用样品采集 | PN-G-04502:2014-11 pkt. 5.3.1.2. | PN-C-06301:1998 | ||
| 108 | Furnace waste, code: ex 20 01 99 (ashes from households) | 化学与物理检测用样品采集 | PN-EN 14899:2005 | ||
| 109 | 固体燃料供暖锅炉 | Condensate sampling for chemical testing | PN-EN 303-5:2021-09 PN-EN 303-5+A1:2023-05 | ||
| 110 | Energy equipment fired with solid fuels | Energy efficiency (calculated) | Procedura Q/LS/01/H:2023 | ||
| 111 | Waste gases from heating appliances | Sampling for determinations of dust, organic contaminants, PAH | Procedura Q/LS/02/H:2023 | ||
| 112 | Waste gases from heating appliances | Dust concentration Range: (1,7 – 3750) mg/m3 Gravimetric method | |||
| 113 | Waste gases from heating appliances | Concentration of organic pollutants Range: (1,7 – 3750) mg/m3 (calculated) | |||
| 114 | Waste gases from heating appliances | PAH concentration (naphthalene, acenaphthene, acenaphthylene, fluorene, phenanthrene, anthracene, fluoranthene, pyrene, benzo(a)anthracene, chrysene, benzo(b+k)fluoranthene, benzo(e)pyrene, benzo(a)pyrene, perylene, dibenzo(a,h)anthracene +indeno(1,2,3-cd)pyrene, benzo(g,h,i)perylene). (calculated) | |||
| 115 | Waste gases from the combustion of smokeless solid fuels | Sampling for determinations of dust, organic contaminants, B(a)P | Procedura Q/LS/07/F:2023 | ||
| 116 | Waste gases from the combustion of smokeless solid fuels | Dust concentration: Range: (1,7 – 3750) mg/m3 Gravimetric method | |||
| 117 | Waste gases from the combustion of smokeless solid fuels | Concentration of organic pollutants: Range: (1,7 – 3750) mg/m3 (calculated) | |||
| 118 | Waste gases from the combustion of smokeless solid fuels | B(a)P concentration: Range: (2,5 – 37,5) µg/m3 (calculated) | |||
| 119 | 固体燃料供暖锅炉 | Water temperature Range: (10,0 – 110) oC Resistance method | PN-EN 303-5:2021-09 09 p. 5.2; 5.6.2; 5.6.3; 5.7.2 PN-EN 303-5+A1:2023-05 p. 5.2; 5.6.2; 5.6.3; 5.7.2 wskazane w Rozp. Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 120 | 固体燃料供暖锅炉 | Water mass flow rate Range: (300 – 18300) kg/h (calculated) | PN-EN 303-5:2021-09 09 p.5.2 PN-EN 303-5+A1:2023-05 p.5.2 wskazane w Rozp. Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 121 | 固体燃料供暖锅炉 | Water volume flow rate Range: (0,3 – 18,3) m3/h Electromagnetic method | PN-EN 303-5:2021-09 p.5.2 PN-EN 303-5+A1:2023-05 p.5.2 wskazane w Rozporządzeniu Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 122 | 固体燃料供暖锅炉 | Fuel mass flow rate Range: (0,5 – 300) kg/h (calculated) | PN-EN 303-5:2021-09 p. 5.2 | PN-EN 303-5+A1:2023-05 p. 5.2 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 123 | 固体燃料供暖锅炉 | Flue gas temperature Range: (50,0 – 300) oC Thermoelectric method | PN-EN 303-5:2021-09 p. 5.6.3 PN-EN 303-5+A1:2023-05 p.5.6.3 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 124 | 固体燃料供暖锅炉 | Flue gas pressure Range: (-150 – 50,0) Pa Piezoresistive method | PN-EN 303-5:2021-09 p.5.6.3 PN-EN 303-5+A1:2023-05 p.5.6.3 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 125 | 固体燃料供暖锅炉 | Concentration of oxygen, carbon monoxide, sulphur dioxide, carbon dioxide, volatile organic compounds in flue gases Range: - O (1,0 – 21,0) % 2 Paramagnetic method Range: - CO (12,5 – 56125) mg/m3 - SO (25,0 – 1490) mg/m3 2 - CO (2,0 – 18,5) % 2 NDIR method Range: - OGC (1,0 – 410) mg/m3 Continuous flame ionisation detection method (FID) | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 126 | 固体燃料供暖锅炉 | Dust concentration in flue gases Range: (0,1 – 3400) mg/m3 Gravimetric method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 127 | 固体燃料供暖锅炉 | Concentration of nitrogen monoxide, nitrogen oxides in flue gases Range: - NO (5,0 – 1200) mg/m3 - NO (8,0 – 1500) mg/m3 X Chemiluminescence method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 128 | 固体燃料供暖锅炉 | Emission of carbon monoxide, carbon dioxide, volatile organic compounds, nitrogen monoxide, nitrogen oxides, dust in flue gases (calculated) | PN-EN 303-5:2021-09 p. 5.9.4 PN-EN 303-5+A1:2023-05 p. 5.9.4 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 129 | 固体燃料供暖锅炉 | Ambient air temperature at the test site Range: (10,0 – 50,0) oC Resistance method | PN-EN 303-5:2021-09 p.5.6.1 | PN-EN 303-5+A1:2023-05 p.5.6.1 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 130 | 固体燃料供暖锅炉 | Temperature of external surfaces Range: (10,0 – 200) oC Radiation method | PN-EN 303-5:2021-09 p.5.11 | PN-EN 303-5+A1:2023-05 p.5.11 | ||
| 131 | 固体燃料供暖锅炉 | Active electrical power Range: (0,001 – 0,5) kW Power transducer method | PN-EN 303-5:2021-09 p.5.7.7 PN-EN 303-5+A1:2023-05 p.5.7.7 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) PN-EN 15456:2008 | ||
| 132 | 固体燃料供暖锅炉 | Testing of the operation of the temperature controller and of the safety temperature limiter Outlet water temperature Range: (10,0 – 110) oC Resistance method | PN-EN 303-5:2021-09 p.5.13 PN-EN 303-5+A1:2023-05 p.5.13 | ||
| 133 | 固体燃料供暖锅炉 | Testing of the operation of fast shut-off systems Water temperature Range: (10,0 – 110) oC Resistance method Flue gas pressure Range: (-150 – 50,0) Pa Piezoresistive method Carbon monoxide concentration Range: CO (12,5 – 56125) mg/m3 NDIR method | PN-EN 303-5:2021-09 p.5.14 PN-EN 303-5+A1:2023-05 p.5.14 | ||
| 134 | 固体燃料供暖锅炉 | Safety testing in the event of loss of air supply Carbon monoxide concentration Range: CO (12,5 – 56125) mg/m3 NDIR method | PN-EN 303-5:2021-09 p.5.16.3 PN-EN 303-5+A1:2023-05 p.5.16.3 | ||
| 135 | 固体燃料供暖锅炉 | Safety testing with regard to heat conduction External surface temperature Range: (10,0 – 200) oC Radiation method | PN-EN 303-5:2021-09 p.5.16.4 PN-EN 303-5+A1:2023-05 p.5.16.4 | ||
| 136 | 固体燃料供暖锅炉 | Determination of water flow resistance Range: Water pressure (0,1 – 100,0) mbar Pressure transducer method Range: Water temperature (10,0 – 110) oC Resistance method | PN-EN 303-5:2021-09 p.5.10 PN-EN 303-5+A1:2023-05 p.5.10 | ||
| 137 | 固体燃料供暖锅炉 | Safety testing of automatic boilers under fuel overfill conditions and with the fuel feed blocked Range: Water temperature (10,0 – 110) oC Resistance method Carbon monoxide concentration Range: CO (12,5 – 56125) mg/m3 NDIR method | PN-EN 303-5:2021-09 p.5.16.2 PN-EN 303-5+A1:2023-05 p.5.16.2 | ||
| 138 | 固体燃料供暖锅炉 | Useful efficiency GCV (calculated) | PN-EN 303-5:2021-09 PN-EN 303-5+A1:2023-05 Rozporządzenie UE 2015/1187 Rozporządzenie UE 2015/1189 | ||
| 139 | 固体燃料供暖锅炉 | Seasonal space heating efficiency (calculated) | |||
| 140 | 固体燃料供暖锅炉 | Energy efficiency index EEI (calculated) | |||
| 141 | 固体燃料供暖锅炉 | Seasonal space heating emissions Es (calculated) | |||
| 142 | Solid fuel heating boilers and energy equipment fired with solid fuels | Heat input from fuel Range: (3 – 750) kW (calculated) | PN-EN 303-5:2021-09 p.5.6.1 | PN-EN 303-5+A1:2023-05 p.5.6.1 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 143 | Solid fuel heating boilers and energy equipment fired with solid fuels | Heat output Range: (3 – 550 ) kW (calculated) | PN-EN 303-5:2021-09 p.5.6.1 | PN-EN 303-5+A1:2023-05 p.5.6.1 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 144 | Solid fuel heating boilers and energy equipment fired with solid fuels | Energy efficiency (calculated) | PN-EN 303-5:2021-09 p.5.7.6 | PN-EN 303-5+A1:2023-05 p.5.7.6 | eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) | ||
| 145 | 废气 | Gas volume flow rate for dynamic pressures > 10 Pa Pitot tube method | PN-Z-04030-7:1994 | ||
| 146 | 废气 | 粉尘浓度测定采样 | |||
| 147 | 废气 | Dust concentration Range: (0,001 – 100) g/m3 Gravimetric method | |||
| 148 | 废气 | 粉尘排放量（计算值） | |||
| 149 | 废气 | Concentration of oxygen, carbon monoxide, nitrogen monoxide, sulphur dioxide, carbon dioxide Range: - O (1,0 – 21,0) % 2 Paramagnetic method - CO (12,5 – 56125) mg/m3 - NO (50,0 – 650) mg/m3 - SO (25,0 – 1490) mg/m3 2 - CO (2,0 – 18,5) % 2 NDIR method | PN-ISO 10396:2001 | ||
| 150 | 废气 | Emission of CO, NO (calculated as NO ), SO CO 2 2, 2 (calculated) | |||
| 151 | 废气 | Concentration of nitrogen monoxide, nitrogen oxides Range: - NO (5,0 – 1200) mg/m3 - NO (8,0 – 1500) mg/m3 X Chemiluminescence method | |||
| 152 | 废气 | Emission of NO NO (NO calculated , X as NO ), SO CO 2 2, 2 (calculated) | |||
| 153 | 颗粒燃料房间加热器 | Fuel parameters: | |||
| 154 | 颗粒燃料房间加热器 | - fuel mass (0,1 - 50) kg | PN-EN 14785:2009 p. A3 | ||
| 155 | 颗粒燃料房间加热器 | Flue gas parameters: | |||
| 156 | 颗粒燃料房间加热器 | - temperature (50 – 300) oC | PN-EN 14785:2009 p. A2.3.2 | ||
| 157 | 颗粒燃料房间加热器 | - pressure (-150 – 50) Pa | PN-EN 14785:2009 p. A2.3.4 | ||
| 158 | 颗粒燃料房间加热器 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O (1,0 – 21,0) % 2 Paramagnetic PMD method - CO (12,5 – 56125) mg/m3 - CO (2,0 – 18,5) % 2 NDIR method | PN-EN 14785:2009 p. A2.3.3 | ||
| 159 | 颗粒燃料房间加热器 | OGC and sulfur dioxide concentration Range: - OGC (1,0 – 410) mg/m3 Continuous flame ionization detection method (FID) - SO (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 160 | 颗粒燃料房间加热器 | Concentration of nitrogen oxide, nitrogen oxides in flue gases Range: - NO (5,0 – 1200) mg/m3 - NOx (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 161 | 颗粒燃料房间加热器 | Dust concentration in flue gases Range: - Dust (0,1 – 3400) mg/m3 Gravimetric method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 162 | 颗粒燃料房间加热器 | Emission of carbon monoxide, carbon dioxide, volatile organic compounds, nitrogen monoxide, nitrogen oxides, dust in flue gases (calculated) | PN-EN 303-5:2021-09 p.5.9.4 PN-EN 303-5+A1:2023-05 p.5.9.4 | ||
| 163 | 颗粒燃料房间加热器 | Air parameters: | |||
| 164 | 颗粒燃料房间加热器 | Air temperature Range: - Temperature (10,0 – 50,0) oC Resistance method | PN-EN 14785:2009 p. A1.1 | ||
| 165 | 颗粒燃料房间加热器 | Water parameters: | |||
| 166 | 颗粒燃料房间加热器 | Water temperature - Temperature (10,0 – 110) oC Resistance method | PN-EN 14785:2009 p. A2.5 | ||
| 167 | 颗粒燃料房间加热器 | Water volume flow rate - Volume flow rate (0,3 – 3) m3/h | PN-EN 14785:2009 p. A2.5 | ||
| 168 | 颗粒燃料房间加热器 | Heat balance (calculated): | |||
| 169 | 颗粒燃料房间加热器 | - heat input from fuel (2 – 100) kW | PN-EN 14785:2009 p. A6.2.2 „N” | ||
| 170 | 颗粒燃料房间加热器 | - stack loss (5 – 40) % | PN-EN 14785:2009 p. A6.2.1.1 „N” | ||
| 171 | 颗粒燃料房间加热器 | - incomplete combustion losses | PN-EN 14785:2009 p. A6.2.1.2 „N” | ||
| 172 | 颗粒燃料房间加热器 | - unburnt combustible losses | PN-EN 14785:2009 p. A6.2.1.3 „N” | ||
| 173 | 颗粒燃料房间加热器 | - thermal efficiency (20 – 95) % | PN-EN 14785:2009 p. A6.2.1 „N” | ||
| 174 | 颗粒燃料房间加热器 | - total heat output (2 – 50) kW | PN-EN 14785:2009 p. A6.2.2 „N” | ||
| 175 | 颗粒燃料房间加热器 | - heat output of the water circuit (2 – 50) kW | PN-EN 14785:2009 p. A6.2.3 „N” | ||
| 176 | 颗粒燃料房间加热器 | - heat output to the room (2 – 50) kW | PN-EN 14785:2009 p. A6.2.4 „N” | ||
| 177 | 颗粒燃料房间加热器 | - flue gas mass flow rate (5 – 100) g/s | PN-EN 14785:2009 p. A6.2.5 „N” | ||
| 178 | 颗粒燃料房间加热器 | - CO content (O =13%) 2 (0,001 – 3) % | PN-EN 14785:2009 p. A6.2.6 „N” | ||
| 179 | 颗粒燃料房间加热器 | Technical and operational parameters: | |||
| 180 | 颗粒燃料房间加热器 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 14785:2009 p. A2.2 | ||
| 181 | 颗粒燃料房间加热器 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 14785:2009 p. A2.2 | ||
| 182 | 颗粒燃料房间加热器 | - temperature of the handles (10,0 – 200) oC | PN-EN 14785:2009 p. A2.2 | ||
| 183 | 颗粒燃料房间加热器 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 14785:2009 p. A4.9.2 „N” | ||
| 184 | 颗粒燃料房间加热器 | - thermal discharge safety device water temperature (10,0 – 110) oC - water pressure (0,05 – 0,5) MPa | PN-EN 14785:2009 p. A4.9.3 „N” | ||
| 185 | 固体燃料嵌入式器具，含明火式壁炉 | Fuel parameters: | |||
| 186 | 固体燃料嵌入式器具，含明火式壁炉 | - fuel mass (0,1 – 50) kg | PN-EN 13229:2002 p. A4.2 „N” | ||
| 187 | 固体燃料嵌入式器具，含明火式壁炉 | Flue gas parameters: | |||
| 188 | 固体燃料嵌入式器具，含明火式壁炉 | - temperature (50 – 300) oC | PN-EN 13229:2002 A4.4.3 „N” | ||
| 189 | 固体燃料嵌入式器具，含明火式壁炉 | - pressure (-150 – 50) Pa | PN-EN 13229:2002 p. A2.3.4 | ||
| 190 | 固体燃料嵌入式器具，含明火式壁炉 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O (1,0 – 21,0) % 2 Paramagnetic PMD method - CO (12,5 – 56125) mg/m3 - CO (2,0 – 18,5) % 2 NDIR method | PN-EN 13229:2002 p. A4.4.2 „N” | ||
| 191 | 固体燃料嵌入式器具，含明火式壁炉 | OGC and sulfur dioxide concentration Range: - OGC (1,0 – 410) mg/m3 Continuous flame ionization detection method (FID) - SO (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 192 | 固体燃料嵌入式器具，含明火式壁炉 | Concentration of nitrogen oxide, nitrogen oxides in flue gases Range: - NO (5,0 – 1200) mg/m3 - NOx (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 193 | 固体燃料嵌入式器具，含明火式壁炉 | Dust concentration in flue gases Range: - Dust (0,1 – 3400) mg/m3 Gravimetric method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 194 | 固体燃料嵌入式器具，含明火式壁炉 | Emission of carbon monoxide, carbon dioxide, volatile organic compounds, nitrogen monoxide, nitrogen oxides, dust in flue gases (calculated) | PN-EN 303-5:2021-09 p.5.9.4 PN-EN 303-5+A1:2023-05 p.5.9.4 | ||
| 195 | 固体燃料嵌入式器具，含明火式壁炉 | Air parameters: | |||
| 196 | 固体燃料嵌入式器具，含明火式壁炉 | Air temperature Range: - Temperature (10,0 – 50,0) oC Resistance method | PN-EN 13229:2002 p. A4.4.3 „N” | ||
| 197 | 固体燃料嵌入式器具，含明火式壁炉 | Water parameters: | |||
| 198 | 固体燃料嵌入式器具，含明火式壁炉 | Water temperature - Temperature (10,0 – 110) oC Resistance method | PN-EN 13229:2002 p. A4.5.2 „N” | ||
| 199 | 固体燃料嵌入式器具，含明火式壁炉 | Water volume flow rate - Volume flow rate (0,3 – 3) m3/h | PN-EN 13229:2002 p. A4.5.2 „N” | ||
| 200 | 固体燃料嵌入式器具，含明火式壁炉 | Heat balance (calculated): | |||
| 201 | 固体燃料嵌入式器具，含明火式壁炉 | - heat input from fuel (2 – 100) kW | PN-EN 13229:2002 p. A6.2.2 „N” | ||
| 202 | 固体燃料嵌入式器具，含明火式壁炉 | - stack loss (5 – 40) % | PN-EN 13229:2002 p. A6.2.1.1 „N” | ||
| 203 | 固体燃料嵌入式器具，含明火式壁炉 | - incomplete combustion losses | PN-EN 13229:2002 p. A6.2.1.2 „N” | ||
| 204 | 固体燃料嵌入式器具，含明火式壁炉 | - unburnt combustible losses | PN-EN 13229:2002 p. A6.2.1.3 „N” | ||
| 205 | 固体燃料嵌入式器具，含明火式壁炉 | - thermal efficiency (20 – 95) % | PN-EN 13229:2002 p. A6.2.1 „N” | ||
| 206 | 固体燃料嵌入式器具，含明火式壁炉 | - total heat output (2 – 50) kW | PN-EN 13229:2002 p. A6.2.2 „N” | ||
| 207 | 固体燃料嵌入式器具，含明火式壁炉 | - heat output of the water circuit (2 – 50) kW | PN-EN 13229:2002 p. A6.2.3 „N” | ||
| 208 | 固体燃料嵌入式器具，含明火式壁炉 | - heat output to the room (2 – 50) kW | PN-EN 13229:2002 p. A6.2.4 „N” | ||
| 209 | 固体燃料嵌入式器具，含明火式壁炉 | - CO content (O =13%) 2 (0,001 – 3) % | PN-EN 13229:2002 p. A6.2.6 „N” | ||
| 210 | 固体燃料嵌入式器具，含明火式壁炉 | Technical and operational parameters: | |||
| 211 | 固体燃料嵌入式器具，含明火式壁炉 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 13229:2002 p. A4.7 | ||
| 212 | 固体燃料嵌入式器具，含明火式壁炉 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 13229:2002 p. A4.7 | ||
| 213 | 固体燃料嵌入式器具，含明火式壁炉 | - temperature of the handles (10,0 – 200) oC | PN-EN 13229:2002 p. A4.7 | ||
| 214 | 固体燃料嵌入式器具，含明火式壁炉 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 13229:2002 p. A4.9.5 „N” | ||
| 215 | 固体燃料嵌入式器具，含明火式壁炉 | - thermal outlet protection water temperature (10,0-110) oC - water pressure (0,05 – 0,5) MPa | PN-EN 13229:2002 p. A4.9.6 „N” | ||
| 216 | 固体燃料房间加热器 | Fuel parameters: | |||
| 217 | 固体燃料房间加热器 | - fuel mass (0,1 - 50) kg | PN-EN 13240:2008 p. A4.2 „N” | ||
| 218 | 固体燃料房间加热器 | Flue gas parameters: | |||
| 219 | 固体燃料房间加热器 | - temperature (50 – 300) oC | PN-EN 13240:2008 A4.4.3 „N” | ||
| 220 | 固体燃料房间加热器 | - pressure (-150 – 50) Pa | PN-EN 13240:2008 p. A2.3.4 | ||
| 221 | 固体燃料房间加热器 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O (1,0 – 21,0) % 2 Paramagnetic PMD method - CO (12,5 – 56125) mg/m3 - CO (2,0 – 18,5) % 2 NDIR method | PN-EN 13240:2008 p. A4.4.2 „N” | ||
| 222 | 固体燃料房间加热器 | OGC and sulfur dioxide concentration Range: - OGC (1,0 – 410) mg/m3 Continuous flame ionization detection method (FID) - SO (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 223 | 固体燃料房间加热器 | Concentration of nitrogen oxide, nitrogen oxides in flue gases Range: - NO (5,0 – 1200) mg/m3 - NOx (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 224 | 固体燃料房间加热器 | Dust concentration in flue gases Range: - Dust (0,1-3400) mg/m3 Gravimetric method | PN-EN 303-5:2021-09 p.5.2 | PN-EN 303-5+A1:2023-05 p.5.2 | ||
| 225 | 固体燃料房间加热器 | Emission of carbon monoxide, carbon dioxide, volatile organic compounds, nitrogen monoxide, nitrogen oxides, dust in flue gases Calculation method | PN-EN 303-5:2021 p.5.9.4 PN-EN 303-5+A1:2023-05 p.5.9.4 | ||
| 226 | 固体燃料房间加热器 | Air parameters: | |||
| 227 | 固体燃料房间加热器 | Air temperature Range: - Temperature (10,0 – 50,0) oC Resistance method | PN-EN 13240:2008 p. A4.4.3 „N” | ||
| 228 | 固体燃料房间加热器 | Water parameters: | |||
| 229 | 固体燃料房间加热器 | Water temperature - Temperature (10,0 – 110) oC Resistance method | PN-EN 13240:2008 p. A4.5.2 „N” | ||
| 230 | 固体燃料房间加热器 | Water volume flow rate - Volume flow rate (0,3 – 3) m3/h | PN-EN 13240:2008 p. A4.5.2 „N” | ||
| 231 | 固体燃料房间加热器 | Heat balance (calculated): | |||
| 232 | 固体燃料房间加热器 | - heat input from fuel (2 – 100) kW | PN-EN 13240:2008 p. A6.2.2 „N” | ||
| 233 | 固体燃料房间加热器 | - stack loss (5 – 40) % | PN-EN 13240:2008 p. A6.2.1.1 „N” | ||
| 234 | 固体燃料房间加热器 | - incomplete combustion losses | PN-EN 13240:2008 p. A6.2.1.2 „N” | ||
| 235 | 固体燃料房间加热器 | - unburnt combustible losses | PN-EN 13240:2008 p. A6.2.1.3 „N” | ||
| 236 | 固体燃料房间加热器 | - thermal efficiency (20 – 95) % | PN-EN 13240:2008 p. A6.2.1 „N” | ||
| 237 | 固体燃料房间加热器 | - total heat output (2 – 50) kW | PN-EN 13240:2008 p. A6.2.2 „N” | ||
| 238 | 固体燃料房间加热器 | - heat output of the water circuit (2 – 50) kW | PN-EN 13240:2008 p. A6.2.3 „N” | ||
| 239 | 固体燃料房间加热器 | - heat output to the room (2 – 50) kW | PN-EN 13240:2008 p. A6.2.4 „N” | ||
| 240 | 固体燃料房间加热器 | - CO content (O =13%) 2 (0,001 – 3) % | PN-EN 13240:2008 p. A6.2.6 „N” | ||
| 241 | 固体燃料房间加热器 | Technical and operational parameters: | |||
| 242 | 固体燃料房间加热器 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 13240:2008 p. A4.7 | ||
| 243 | 固体燃料房间加热器 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 13240:2008 p. A4.7 | ||
| 244 | 固体燃料房间加热器 | - temperature of the handles (10,0 – 200) oC | PN-EN 13240:2008 p. A4.7 | ||
| 245 | 固体燃料房间加热器 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 13240:2008 p. A4.9.4 „N” | ||
| 246 | 固体燃料房间加热器 | - thermal outlet protection water temperature (10,0-110) oC - water pressure (0,05 – 0,5) MPa | PN-EN 13240:2008 p. A4.9.5 „N” | ||
| 247 | 民用固体燃料燃烧器具 | Fuel parameters: | |||
| 248 | 民用固体燃料燃烧器具 | - fuel mass (0,1 - 50) kg | PN-EN 16510-1:2018 p. A4.2 PN-EN 16510-1:2023-06 p.A4.2 | ||
| 249 | 民用固体燃料燃烧器具 | Flue gas parameters: | |||
| 250 | 民用固体燃料燃烧器具 | - temperature (50 – 300) oC | PN-EN 16510-1:2018 A4.4.3 PN-EN 16510-1:2023-06 A4.4.3 | ||
| 251 | 民用固体燃料燃烧器具 | - pressure (-150 – 50) Pa | PN-EN 16510-1:2018 p. A2.3.4 | PN-EN 16510-1:2023-06 p. A2.3.4 | ||
| 252 | 民用固体燃料燃烧器具 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O (1,0 – 21,0) % 2 Paramagnetic PMD method - CO (12,5 – 56125) mg/m3 - CO (2,0 – 18,5) % 2 NDIR method | PN-EN 16510-1:2018 p. A.4.4.2 | PN-EN 16510-1:2023-06 p. A.4.4.2 | ||
| 253 | 民用固体燃料燃烧器具 | OGC and sulfur dioxide concentration Range: - OGC (1,0 – 410) mg/m3 Continuous flame ionization detection method (FID) - SO (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 16510-1:2018 p. A.4.4.2 | PN-EN 16510-1:2023-06 p.A.4.4.2 | ||
| 254 | 民用固体燃料燃烧器具 | Concentration of nitrogen oxide, nitrogen oxides in flue gases Range: - NO (5,0 – 1200) mg/m3 - NOx (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 16510-1:2018 p. A.4.4.2 | PN-EN 16510-1:2023-06 p. A.4.4.2 | ||
| 255 | 民用固体燃料燃烧器具 | Dust concentration in flue gases Range: - Dust (1,7 – 3750) mg/m3 Gravimetric method | PN-EN 16510-1:2018 p. A.4.4.2 PN-EN 16510-1:2023-06 p. A.4.4.2 Załącznik F | ||
| 256 | 民用固体燃料燃烧器具 | Emission of carbon monoxide, carbon dioxide, volatile organic compounds, nitrogen monoxide, nitrogen oxides, dust in flue gases Calculation method | PN-EN 16510-1:2018 p. A.4.4.2 | PN-EN 16510-1:2023-06 p. A.4.4.2 | ||
| 257 | 民用固体燃料燃烧器具 | Air parameters: | |||
| 258 | 民用固体燃料燃烧器具 | Air temperature Range: - Temperature (10,0 – 50,0) oC Resistance method | PN-EN 16510-1:2018 p. A4.4.3 PN-EN 16510-1:2023-06 p. A4.4.3 | ||
| 259 | 民用固体燃料燃烧器具 | Water parameters: | |||
| 260 | 民用固体燃料燃烧器具 | Water temperature - Temperature (10,0 – 110) oC Resistance method | PN-EN 16510-1:2018 p. A4.5.2 PN-EN 16510-1:2023-06 p. A4.5.2 | ||
| 261 | 民用固体燃料燃烧器具 | Water volume flow rate - Volume flow rate (0,3 – 3) m3/h | PN-EN 16510-1:2018 p. A4.5.2 PN-EN 16510-1:2023-06 p. A4.5.2 | ||
| 262 | 民用固体燃料燃烧器具 | Heat balance (calculated): | |||
| 263 | 民用固体燃料燃烧器具 | - heat input from fuel (2 – 100) kW | PN-EN 16510-1:2018 p. A6.2.2 PN-EN 16510-1:2023-06 p.A6.2.2 | ||
| 264 | 民用固体燃料燃烧器具 | - stack loss (5 – 40) % | PN-EN 16510-1:2018 p.A6.2.1.2 PN-EN 16510-1:2023-06 p.A6.2.1.2 | ||
| 265 | 民用固体燃料燃烧器具 | - incomplete combustion losses | PN-EN 16510-1:2018 p.A6.2.1.3 PN-EN 16510-1:2023-06 p.A6.2.1.3 | ||
| 266 | 民用固体燃料燃烧器具 | - unburnt combustible losses | PN-EN 16510-1:2018 p.A6.2.1.4 PN-EN 16510-1:2023-06 p.A6.2.1.4 | ||
| 267 | 民用固体燃料燃烧器具 | - thermal efficiency (20 – 95) % | PN-EN 16510-1:2018 p.A6.2.1 PN-EN 16510-1:2023-06 p.A6.2.1 | ||
| 268 | 民用固体燃料燃烧器具 | - total heat output (2 – 50) kW | PN-EN 16510-1:2018 p.A6.2.2 PN-EN 16510-1:2023-06 p.A6.2.2 | ||
| 269 | 民用固体燃料燃烧器具 | - heat output of the water circuit (2 – 50) kW | PN-EN 16510-1:2018 p.A6.2.3 PN-EN 16510-1:2023-06 p.A6.2.3 | ||
| 270 | 民用固体燃料燃烧器具 | - heat output to the room (2 – 50) kW | PN-EN 16510-1:2018 p.A6.2.4 PN-EN 16510-1:2023-06 p.A6.2.4 | ||
| 271 | 民用固体燃料燃烧器具 | - CO content (O =13%) 2 (0,001 – 3) % | PN-EN 16510-1:2018 p.A6.2.6 PN-EN 16510-1:2023-06 p.A6.2.6 | ||
| 272 | 民用固体燃料燃烧器具 | Technical and operational parameters: | |||
| 273 | 民用固体燃料燃烧器具 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 16510-1:2018 p.A4.7 | PN-EN 16510-1:2023-06 p.A4.7 | ||
| 274 | 民用固体燃料燃烧器具 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 16510-1:2018 p.A4.7 | PN-EN 16510-1:2023-06 p.A4.7 | ||
| 275 | 民用固体燃料燃烧器具 | - temperature of the handles (10,0 – 200) oC | PN-EN 16510-1:2018 p. A4.7 | PN-EN 16510-1:2023-06 p.A4.7 | ||
| 276 | 民用固体燃料燃烧器具 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 16510-1:2018 p. A.4.10.5 PN-EN 16510-1:2023-06 p. A.4.10.5 | ||
| 277 | 民用固体燃料燃烧器具 | - thermal outlet protection water temperature (10,0-110) oC - water pressure (0,05 – 0,5) MPa | PN-EN 16510-1:2018 p A.4.10.6 PN-EN 16510-1:2023-06 p A.4.10.6 | ||
| 278 | Liquid fuel fireplaces | Fuel tank capacity | PN-EN 16647:2015-11 | ||
| 279 | Liquid fuel fireplaces | Construction of the device | |||
| 280 | Liquid fuel fireplaces | Construction of the ignition device | |||
| 281 | Liquid fuel fireplaces | Resistance to tilting and sliding | |||
| 282 | Liquid fuel fireplaces | Resistance to displacement of the device caused by the impact of a bag | |||
| 283 | Liquid fuel fireplaces | Resistance to tilting of the device caused by the impact of a bag | |||
| 284 | Liquid fuel fireplaces | Resistance of the device to static loads | |||
| 285 | Liquid fuel fireplaces | Resistance to fuel spillage | |||
| 286 | 民用固体燃料燃烧器具 — 房间加热器 | Fuel parameters: | |||
| 287 | 民用固体燃料燃烧器具 — 房间加热器 | - fuel mass (0,1 - 50) kg | PN-EN 16510-1:2023-06 p. A.4.2 | ||
| 288 | 民用固体燃料燃烧器具 — 房间加热器 | Flue gas parameters: | |||
| 289 | 民用固体燃料燃烧器具 — 房间加热器 | - temperature (50 – 300) oC | PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-1:2023-06 p.4.7.2 | ||
| 290 | 民用固体燃料燃烧器具 — 房间加热器 | - pressure (-150 – 50) Pa | PN-EN 16510-1:2023-06 p. A.2.3.4 | PN-EN 16510-2-1:2023-06 p. 4.7.3 | ||
| 291 | 民用固体燃料燃烧器具 — 房间加热器 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O ; (1,0 – 21,0) % 2 PMD paramagnetic method - CO; (12,5 – 56125) mg/m3 - CO ; (2,0 – 18,5) % 2 NDIR method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-1:2023-06 p. 4.3 „N” | ||
| 292 | 民用固体燃料燃烧器具 — 房间加热器 | Concentration of OGC and sulphur dioxide Range: - OGC; (1,0 – 410) mg/m3 Continuous flame ionisation detection method (FID) - SO ; (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 16510-1:2023-06 p. A.4.4.2 | PN-EN 16510-2-1:2023-06 p. 4.5 „N” | ||
| 293 | 民用固体燃料燃烧器具 — 房间加热器 | Concentration of nitrogen monoxide, nitrogen dioxide, nitrogen oxides in flue gases Range: - NO; (5,0 – 1200) mg/m3 - NOx; (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-1:2023-06 p. 4.4 „N” | ||
| 294 | 民用固体燃料燃烧器具 — 房间加热器 | Dust concentration in flue gases Range: - Dust; (0 – 8500) mg/m3 Gravimetric method | PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-1:2023-06 p. 4.6 „N” | ||
| 295 | 民用固体燃料燃烧器具 — 房间加热器 | Air parameters: | |||
| 296 | 民用固体燃料燃烧器具 — 房间加热器 | Air temperature Range: - Temperature; (10,0 – 50,0) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.4.3 | ||
| 297 | 民用固体燃料燃烧器具 — 房间加热器 | Water parameters: | |||
| 298 | 民用固体燃料燃烧器具 — 房间加热器 | Water temperature - Temperature; (10,0 – 110) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 299 | 民用固体燃料燃烧器具 — 房间加热器 | Water volume flow rate - Volume flow rate; (0,3 – 3) m3/h | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 300 | 民用固体燃料燃烧器具 — 房间加热器 | Heat balance (calculated): | |||
| 301 | 民用固体燃料燃烧器具 — 房间加热器 | - heat input from fuel (2 – 100) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 | ||
| 302 | 民用固体燃料燃烧器具 — 房间加热器 | - stack loss (5 – 40) % | PN-EN 16510-1:2023-06 p. A.6.2.1.2 | ||
| 303 | 民用固体燃料燃烧器具 — 房间加热器 | - incomplete combustion losses | PN-EN 16510-1:2023-06 p. A.6.2.1.3 | ||
| 304 | 民用固体燃料燃烧器具 — 房间加热器 | - unburnt combustible losses | PN-EN 16510-1:2023-06 p. A.6.2.1.4 | ||
| 305 | 民用固体燃料燃烧器具 — 房间加热器 | - thermal efficiency (20 – 95) % | PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-1:2023-06 p. 4.8.3 | ||
| 306 | 民用固体燃料燃烧器具 — 房间加热器 | - total heat output (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-1:2023-06 p. 4.8.1 | ||
| 307 | 民用固体燃料燃烧器具 — 房间加热器 | - heat output of the water circuit (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-1:2023-06 p. 4.8.2 | ||
| 308 | 民用固体燃料燃烧器具 — 房间加热器 | - heat output to the room (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.4 | ||
| 309 | 民用固体燃料燃烧器具 — 房间加热器 | - CO content (O =13%) (0,001 – 3) 2 % | PN-EN 16510-1:2023-06 p. A.6.2.6 | ||
| 310 | 民用固体燃料燃烧器具 — 房间加热器 | Technical and operational parameters: | |||
| 311 | 民用固体燃料燃烧器具 — 房间加热器 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 16510-1:2023-06 p. A.4.7 | ||
| 312 | 民用固体燃料燃烧器具 — 房间加热器 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-1:2023-06 p. 5.5 „N” | ||
| 313 | 民用固体燃料燃烧器具 — 房间加热器 | - temperature of the handles (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-1:2023-06 p.5.6 „N” | ||
| 314 | 民用固体燃料燃烧器具 — 房间加热器 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-1:2023-06 p. 5.3 „N” | ||
| 315 | 民用固体燃料燃烧器具 — 房间加热器 | - thermal outlet protection water temperature (10,0-110) oC water pressure (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.7 | ||
| 316 | 民用固体燃料燃烧器具 — 房间加热器 | - measurement of electrical energy consumption (1 – 500) W Method: power transducer | PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-1:2023-06 p. 4.8.9 | ||
| 317 | 民用固体燃料燃烧器具 — 房间加热器 | - efficiency (calculated) - seasonal space heating efficiency (calculated) - energy efficiency index EEI (calculated) | PN-EN 16510-1:2023-06 p A.6.2.1.5 | PN-EN 16510-2-1:2023-06 p. 4.8.7 | ||
| 318 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Fuel parameters: | |||
| 319 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - fuel mass (0,1 - 50) kg | PN-EN 16510-1:2023-06 p. A.4.2 | ||
| 320 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Flue gas parameters: | |||
| 321 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - temperature (50 – 300) oC | PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-2:2023-06 p.4.6.2 | ||
| 322 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - pressure (-150 – 50) Pa | PN-EN 16510-1:2023-06 p. A.2.3.4 | PN-EN 16510-2-2:2023-06 p.4.6.4 | ||
| 323 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O ; (1,0 – 21,0) % 2 PMD paramagnetic method - CO; (12,5 – 56125) mg/m3 - CO ; (2,0 – 18,5) % 2 NDIR method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-2:2023-06 p. 4.2 „N” | ||
| 324 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Concentration of OGC and sulphur dioxide Range: - OGC; (1,0 – 410) mg/m3 Continuous flame ionisation detection method (FID) - SO ; (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 16510-1:2023-06 p. A.4.4.2 | PN-EN 16510-2-2:2023-06 p. 4.4 „N” | ||
| 325 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Concentration of nitrogen monoxide, nitrogen dioxide, nitrogen oxides in flue gases Range: - NO; (5,0 – 1200) mg/m3 - NOx; (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-2:2023-06 p. 4.3 „N” | ||
| 326 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Dust concentration in flue gases Range: - Dust; (0 – 8500) mg/m3 Gravimetric method | PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-2:2023-06 p. 4.5 „N” | ||
| 327 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Air parameters: | |||
| 328 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Air temperature Range: - Temperature; (10,0 – 50,0) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.4.3 | ||
| 329 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Water parameters: | |||
| 330 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Water temperature - Temperature; (10,0 – 110) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 331 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Water volume flow rate - Volume flow rate; (0,3 – 3) m3/h | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 332 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Heat balance (calculated): | |||
| 333 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - heat input from fuel (2 – 100) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 | ||
| 334 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - stack loss (5 – 40) % | PN-EN 16510-1:2023-06 p. A.6.2.1.2 | ||
| 335 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - incomplete combustion losses | PN-EN 16510-1:2023-06 p. A.6.2.1.3 | ||
| 336 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - unburnt combustible losses | PN-EN 16510-1:2023-06 p. A.6.2.1.4 | ||
| 337 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - thermal efficiency (20 – 95) % | PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-2:2023-06 p. 4.7.3 | ||
| 338 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - total heat output (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-2:2023-06 p. 4.7.1 | ||
| 339 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - heat output of the water circuit (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-2:2023-06 p. 4.7.2 | ||
| 340 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - heat output to the room (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.4 | ||
| 341 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - CO content (O =13%) (0,001 – 3) 2 % | PN-EN 16510-1:2023-06 p. A.6.2.6 | ||
| 342 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | Technical and operational parameters: | |||
| 343 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 16510-1:2023-06 p. A.4.7 | ||
| 344 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-2:2023-06 p. 5.5 „N” | ||
| 345 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - temperature of the handles (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-2:2023-06 p.5.6 „N” | ||
| 346 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-2:2023-06 p. 5.3.3 „N” | ||
| 347 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - thermal outlet protection water temperature (10,0-110) oC water pressure (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.7 | ||
| 348 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - measurement of electrical energy consumption (1 – 500) W Method: power transducer | PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-2:2023-06 p. 4.7.9 | ||
| 349 | 民用固体燃料燃烧器具 — 嵌入式器具，含明火式 | - efficiency (calculated) - seasonal space heating efficiency (calculated) - energy efficiency index EEI (calculated) | PN-EN 16510-1:2023-06 p A.6.2.1.5 | PN-EN 16510-2-2:2023-06 p. 4.7.7 | ||
| 350 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Fuel parameters: | |||
| 351 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - fuel mass (0,1 - 50) kg | PN-EN 16510-1:2023-06 p. A.4.2 | ||
| 352 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Flue gas parameters: | |||
| 353 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - temperature (50 – 300) oC | PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-6:2023-06 p.4.7.2 | ||
| 354 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - pressure (-150 – 50) Pa | PN-EN 16510-1:2023-06 p. A.2.3.4 | PN-EN 16510-2-6:2023-06 p.4.7.4 | ||
| 355 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Concentration of oxygen, carbon monoxide and carbon dioxide Range: - O ; (1,0 – 21,0) % 2 PMD paramagnetic method - CO; (12,5 – 56125) mg/m3 - CO ; (2,0 – 18,5) % 2 NDIR method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-6:2023-06 p. 4.3 „N” | ||
| 356 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Concentration of OGC and sulphur dioxide Range: - OGC; (1,0 – 410) mg/m3 Continuous flame ionisation detection method (FID) - SO ; (25,0 - 1490) mg/m3 2 NDIR method | PN-EN 16510-1:2023-06 p. A.4.4.2 | PN-EN 16510-2-6:2023-06 p. 4.5 „N” | ||
| 357 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Concentration of nitrogen monoxide, nitrogen dioxide, nitrogen oxides in flue gases Range: - NO; (5,0 – 1200) mg/m3 - NOx; (8,0 – 1500) mg/m3 Chemiluminescence method | PN-EN 16510-1: 2023-06 p. A.4.4.2 | PN-EN 16510-2-6:2023-06 p. 4.4 „N” | ||
| 358 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Dust concentration in flue gases Range: - Dust; (0 – 8500) mg/m3 Gravimetric method | PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-6:2023-06 p. 4.6 „N” | ||
| 359 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Air parameters: | |||
| 360 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Air temperature Range: - Temperature; (10,0 – 50,0) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.4.3 | ||
| 361 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Water parameters: | |||
| 362 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Water temperature - Temperature; (10,0 – 110) oC Resistance method | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 363 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Water volume flow rate - Volume flow rate; (0,3 – 3) m3/h | PN-EN 16510-1:2023-06 p. A.4.5.2 | ||
| 364 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Heat balance (calculated): | |||
| 365 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - heat input from fuel (2 – 100) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 | ||
| 366 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - stack loss (5 – 40) % | PN-EN 16510-1:2023-06 p. A.6.2.1.2 | ||
| 367 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - incomplete combustion losses | PN-EN 16510-1:2023-06 p. A.6.2.1.3 | ||
| 368 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - unburnt combustible losses | PN-EN 16510-1:2023-06 p. A.6.2.1.4 | ||
| 369 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - thermal efficiency (20 – 95) % | PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-6:2023-06 p. 4.8.3 | ||
| 370 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - total heat output (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-6:2023-06 p. 4.8.1 | ||
| 371 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - heat output of the water circuit (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-6:2023-06 p. 4.8.2 | ||
| 372 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - heat output to the room (2 – 50) kW | PN-EN 16510-1:2023-06 p. A.6.2.4 | ||
| 373 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - CO content (O =13%) (0,001 – 3) 2 % | PN-EN 16510-1:2023-06 p. A.6.2.6 | ||
| 374 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | Technical and operational parameters: | |||
| 375 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - temperature of the measuring corner and the floor (10,0 – 150) oC | PN-EN 16510-1:2023-06 p. A.4.7 | ||
| 376 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - temperature of the fuel hopper (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-6:2023-06 p. 5.5.1 | ||
| 377 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - temperature of the handles (10,0 – 200) oC | PN-EN 16510-1:2023-06 p. A.4.7 | PN-EN 16510-2-6:2023-06 p.5.6 „N” | ||
| 378 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - leak tightness of the water space (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-6:2023-06 p. 5.3.3 „N” | ||
| 379 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - thermal outlet protection water temperature (10,0-110) oC water pressure (0,05 – 0,5) MPa | PN-EN 16510-1:2023-06 p. A 4.10.7 | ||
| 380 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - measurement of electrical energy consumption (1 – 500) W Method: power transducer | PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-6:2023-06 p. 4.8.9 | ||
| 381 | 民用固体燃料燃烧器具 — 房间加热器、嵌入式器具及炊具，带木质颗粒机械给料 | - efficiency (calculated), - seasonal space heating efficiency (calculated) - energy efficiency index EEI (calculated) | PN-EN 16510-1:2023-06 p A.6.2.1.5 | PN-EN 16510-2-6:2023-06 p. 4.8.7 | ||
| 382 | 固体燃料： — 烟煤 | Maceral group composition Range: V (10 – 90) % L (0 – 20) % I (0 – 50) % M (0 – 15) % Microscopic method | PN-ISO 7404-3:2001 | ||
| 383 | 固体燃料： — 烟煤 | Vitrinite reflectance Range: (0,50 – 4,00) % Microscopic method | PN-ISO 7404-5:2002 | ||
| 384 | Solid fuels: - coke | Reactivity towards CO 2 and coke strength after reaction Range: CRI (15,0 – 80,0) CSR (0,0 – 80,0) Gravimetric method | PN-C-04312:1996 ASTM D5341 / D5341M-19 ISO 18894:2018 | ||
| 385 | Commission decision number | Product(s) | Zharmonizowane specyfikacje techniczne | ||
| 386 | 99/471/WE | Space heaters fired with solid and liquid fuels | EN 14785:2006 EN 13229:2001 EN 13229:2001/A1:2003 EN 13229:2001/A2:2004 EN 13229:2001/A2:2004/AC:2007 EN 13229:2001/AC:2006 EN 13240:2001 EN 13240:2001/A2:2004 EN 13240:2001/A2:2004/AC:2007 EN 13240:2001/AC:2006 EN 16510-2-1:2022 EN 16510-2-2:2022 EN 16510-2-6:2022 | ||
引用标准 (254)
EN 14785:2006 EN 13229:2001 EN 13229:2001/A1:2003 EN 13229:2001/A2:2004 EN 13229:2001/A2:2004/AC:2007 EN 13229:2001/AC:2006 EN 13240:2001 EN 13240:2001/A2:2004 EN 13240:2001/A2:2004/AC:2007 EN 13240:2001/AC:2006 EN 16510-2-1:2022 EN 16510-2-2:2022 EN 16510-2-6:2022
EN ISO 21404:2020-08
EN/TR 15404:2010
EN/TS 15414-1:2010
ISO 1953:2015 pkt. 6.2
ISO 19579:2006
ISO 5068-1:2007
ISO 5068-2:2007
PN-80/G-04511
PN-80/G-04512+Az1:2002 PN-ISO 1171:2002
PN-81/G-04513 PN-ISO 1928:2020-05
PN-81/G-04517 ISO 349:2020
PN-82/C-97555/03
PN-82/G-04543
PN-83/C-97555/04
PN-84/C-97555/08
PN-84/C-97555/09
PN-88/C-97555/01
PN-90/C-97554 pkt. 5.4.2. PN-EN 12915-1:2009 p. 8.2.3
PN-90/C-97554 pkt. 5.4.5. PN-EN 12915-1:2009 p.8.2.4
PN-93/C-96012 Metoda C
PN-C-04312:1996 ASTM D5341 / D5341M-19 ISO 18894:2018
PN-C-06301:1998
PN-EN 12902:2005 pkt. 6.10
PN-EN 12902:2005 pkt. 6.2
PN-EN 12902:2005 pkt. 6.5
PN-EN 13229:2002 A4.4.3 „N”
PN-EN 13229:2002 p. A2.3.4
PN-EN 13229:2002 p. A4.2 „N”
PN-EN 13229:2002 p. A4.4.2 „N”
PN-EN 13229:2002 p. A4.4.3 „N”
PN-EN 13229:2002 p. A4.5.2 „N”
PN-EN 13229:2002 p. A4.7
PN-EN 13229:2002 p. A4.9.5 „N”
PN-EN 13229:2002 p. A4.9.6 „N”
PN-EN 13229:2002 p. A6.2.1 „N”
PN-EN 13229:2002 p. A6.2.1.1 „N”
PN-EN 13229:2002 p. A6.2.1.2 „N”
PN-EN 13229:2002 p. A6.2.1.3 „N”
PN-EN 13229:2002 p. A6.2.2 „N”
PN-EN 13229:2002 p. A6.2.3 „N”
PN-EN 13229:2002 p. A6.2.4 „N”
PN-EN 13229:2002 p. A6.2.6 „N”
PN-EN 13240:2008 A4.4.3 „N”
PN-EN 13240:2008 p. A2.3.4
PN-EN 13240:2008 p. A4.2 „N”
PN-EN 13240:2008 p. A4.4.2 „N”
PN-EN 13240:2008 p. A4.4.3 „N”
PN-EN 13240:2008 p. A4.5.2 „N”
PN-EN 13240:2008 p. A4.7
PN-EN 13240:2008 p. A4.9.4 „N”
PN-EN 13240:2008 p. A4.9.5 „N”
PN-EN 13240:2008 p. A6.2.1 „N”
PN-EN 13240:2008 p. A6.2.1.1 „N”
PN-EN 13240:2008 p. A6.2.1.2 „N”
PN-EN 13240:2008 p. A6.2.1.3 „N”
PN-EN 13240:2008 p. A6.2.2 „N”
PN-EN 13240:2008 p. A6.2.3 „N”
PN-EN 13240:2008 p. A6.2.4 „N”
PN-EN 13240:2008 p. A6.2.6 „N”
PN-EN 14785:2009 p. A1.1
PN-EN 14785:2009 p. A2.2
PN-EN 14785:2009 p. A2.3.2
PN-EN 14785:2009 p. A2.3.3
PN-EN 14785:2009 p. A2.3.4
PN-EN 14785:2009 p. A2.5
PN-EN 14785:2009 p. A3
PN-EN 14785:2009 p. A4.9.2 „N”
PN-EN 14785:2009 p. A4.9.3 „N”
PN-EN 14785:2009 p. A6.2.1 „N”
PN-EN 14785:2009 p. A6.2.1.1 „N”
PN-EN 14785:2009 p. A6.2.1.2 „N”
PN-EN 14785:2009 p. A6.2.1.3 „N”
PN-EN 14785:2009 p. A6.2.2 „N”
PN-EN 14785:2009 p. A6.2.3 „N”
PN-EN 14785:2009 p. A6.2.4 „N”
PN-EN 14785:2009 p. A6.2.5 „N”
PN-EN 14785:2009 p. A6.2.6 „N”
PN-EN 14899:2005
PN-EN 15408:2011
PN-EN 16510-1: 2023-06 p. A.4.4.2
PN-EN 16510-1:2018 A4.4.3 PN-EN 16510-1:2023-06 A4.4.3
PN-EN 16510-1:2018 p A.4.10.6 PN-EN 16510-1:2023-06 p A.4.10.6
PN-EN 16510-1:2018 p. A.4.10.5 PN-EN 16510-1:2023-06 p. A.4.10.5
PN-EN 16510-1:2018 p. A.4.4.2
PN-EN 16510-1:2018 p. A.4.4.2 PN-EN 16510-1:2023-06 p. A.4.4.2 Załącznik F
PN-EN 16510-1:2018 p. A2.3.4
PN-EN 16510-1:2018 p. A4.2 PN-EN 16510-1:2023-06 p.A4.2
PN-EN 16510-1:2018 p. A4.4.3 PN-EN 16510-1:2023-06 p. A4.4.3
PN-EN 16510-1:2018 p. A4.5.2 PN-EN 16510-1:2023-06 p. A4.5.2
PN-EN 16510-1:2018 p. A4.7
PN-EN 16510-1:2018 p. A6.2.2 PN-EN 16510-1:2023-06 p.A6.2.2
PN-EN 16510-1:2018 p.A4.7
PN-EN 16510-1:2018 p.A6.2.1 PN-EN 16510-1:2023-06 p.A6.2.1
PN-EN 16510-1:2018 p.A6.2.1.2 PN-EN 16510-1:2023-06 p.A6.2.1.2
PN-EN 16510-1:2018 p.A6.2.1.3 PN-EN 16510-1:2023-06 p.A6.2.1.3
PN-EN 16510-1:2018 p.A6.2.1.4 PN-EN 16510-1:2023-06 p.A6.2.1.4
PN-EN 16510-1:2018 p.A6.2.2 PN-EN 16510-1:2023-06 p.A6.2.2
PN-EN 16510-1:2018 p.A6.2.3 PN-EN 16510-1:2023-06 p.A6.2.3
PN-EN 16510-1:2018 p.A6.2.4 PN-EN 16510-1:2023-06 p.A6.2.4
PN-EN 16510-1:2018 p.A6.2.6 PN-EN 16510-1:2023-06 p.A6.2.6
PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-1:2023-06 p.4.7.2
PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-2:2023-06 p.4.6.2
PN-EN 16510-1:2023-06 A.4.4.3 PN-EN 16510-2-6:2023-06 p.4.7.2
PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-1:2023-06 p. 4.6 „N”
PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-2:2023-06 p. 4.5 „N”
PN-EN 16510-1:2023-06 Załącznik F PN-EN 16510-2-6:2023-06 p. 4.6 „N”
PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-1:2023-06 p. 4.8.9
PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-2:2023-06 p. 4.7.9
PN-EN 16510-1:2023-06 p 6.11 PN-EN 16510-2-6:2023-06 p. 4.8.9
PN-EN 16510-1:2023-06 p A.6.2.1.5
PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-1:2023-06 p. 5.3 „N”
PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-2:2023-06 p. 5.3.3 „N”
PN-EN 16510-1:2023-06 p. A 4.10.6 PN-EN 16510-2-6:2023-06 p. 5.3.3 „N”
PN-EN 16510-1:2023-06 p. A 4.10.7
PN-EN 16510-1:2023-06 p. A.2.3.4
PN-EN 16510-1:2023-06 p. A.4.2
PN-EN 16510-1:2023-06 p. A.4.4.2
PN-EN 16510-1:2023-06 p. A.4.4.3
PN-EN 16510-1:2023-06 p. A.4.5.2
PN-EN 16510-1:2023-06 p. A.4.7
PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-1:2023-06 p. 4.8.3
PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-2:2023-06 p. 4.7.3
PN-EN 16510-1:2023-06 p. A.6.2.1 PN-EN 16510-2-6:2023-06 p. 4.8.3
PN-EN 16510-1:2023-06 p. A.6.2.1.2
PN-EN 16510-1:2023-06 p. A.6.2.1.3
PN-EN 16510-1:2023-06 p. A.6.2.1.4
PN-EN 16510-1:2023-06 p. A.6.2.2
PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-1:2023-06 p. 4.8.1
PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-2:2023-06 p. 4.7.1
PN-EN 16510-1:2023-06 p. A.6.2.2 PN-EN 16510-2-6:2023-06 p. 4.8.1
PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-1:2023-06 p. 4.8.2
PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-2:2023-06 p. 4.7.2
PN-EN 16510-1:2023-06 p. A.6.2.3 PN-EN 16510-2-6:2023-06 p. 4.8.2
PN-EN 16510-1:2023-06 p. A.6.2.4
PN-EN 16510-1:2023-06 p. A.6.2.6
PN-EN 16510-1:2023-06 p. A2.3.4
PN-EN 16510-1:2023-06 p.A.4.4.2
PN-EN 16510-1:2023-06 p.A4.7
PN-EN 16510-2-1:2023-06 p. 4.3 „N”
PN-EN 16510-2-1:2023-06 p. 4.4 „N”
PN-EN 16510-2-1:2023-06 p. 4.5 „N”
PN-EN 16510-2-1:2023-06 p. 4.7.3
PN-EN 16510-2-1:2023-06 p. 4.8.7
PN-EN 16510-2-1:2023-06 p. 5.5 „N”
PN-EN 16510-2-1:2023-06 p.5.6 „N”
PN-EN 16510-2-2:2023-06 p. 4.2 „N”
PN-EN 16510-2-2:2023-06 p. 4.3 „N”
PN-EN 16510-2-2:2023-06 p. 4.4 „N”
PN-EN 16510-2-2:2023-06 p. 4.7.7
PN-EN 16510-2-2:2023-06 p. 5.5 „N”
PN-EN 16510-2-2:2023-06 p.4.6.4
PN-EN 16510-2-2:2023-06 p.5.6 „N”
PN-EN 16510-2-6:2023-06 p. 4.3 „N”
PN-EN 16510-2-6:2023-06 p. 4.4 „N”
PN-EN 16510-2-6:2023-06 p. 4.5 „N”
PN-EN 16510-2-6:2023-06 p. 4.8.7
PN-EN 16510-2-6:2023-06 p. 5.5.1
PN-EN 16510-2-6:2023-06 p.4.7.4
PN-EN 16510-2-6:2023-06 p.5.6 „N”
PN-EN 16647:2015-11
PN-EN 303-5+A1:2023-05 p. 5.2
PN-EN 303-5+A1:2023-05 p.5.11
PN-EN 303-5+A1:2023-05 p.5.2
PN-EN 303-5+A1:2023-05 p.5.6.1
PN-EN 303-5+A1:2023-05 p.5.7.6
PN-EN 303-5:2021 p.5.9.4 PN-EN 303-5+A1:2023-05 p.5.9.4
PN-EN 303-5:2021-09 09 p. 5.2; 5.6.2; 5.6.3; 5.7.2 PN-EN 303-5+A1:2023-05 p. 5.2; 5.6.2; 5.6.3; 5.7.2 wskazane w Rozp. Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 09 p.5.2 PN-EN 303-5+A1:2023-05 p.5.2 wskazane w Rozp. Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 PN-EN 303-5+A1:2023-05
PN-EN 303-5:2021-09 PN-EN 303-5+A1:2023-05 Rozporządzenie UE 2015/1187 Rozporządzenie UE 2015/1189
PN-EN 303-5:2021-09 p. 5.2
PN-EN 303-5:2021-09 p. 5.6.3 PN-EN 303-5+A1:2023-05 p.5.6.3 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 p. 5.9.4 PN-EN 303-5+A1:2023-05 p. 5.9.4 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 p.5.10 PN-EN 303-5+A1:2023-05 p.5.10
PN-EN 303-5:2021-09 p.5.11
PN-EN 303-5:2021-09 p.5.13 PN-EN 303-5+A1:2023-05 p.5.13
PN-EN 303-5:2021-09 p.5.14 PN-EN 303-5+A1:2023-05 p.5.14
PN-EN 303-5:2021-09 p.5.16.2 PN-EN 303-5+A1:2023-05 p.5.16.2
PN-EN 303-5:2021-09 p.5.16.3 PN-EN 303-5+A1:2023-05 p.5.16.3
PN-EN 303-5:2021-09 p.5.16.4 PN-EN 303-5+A1:2023-05 p.5.16.4
PN-EN 303-5:2021-09 p.5.2
PN-EN 303-5:2021-09 p.5.2 PN-EN 303-5+A1:2023-05 p.5.2 wskazane w Rozporządzeniu Ministra Rozwoju i Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 p.5.6.1
PN-EN 303-5:2021-09 p.5.6.3 PN-EN 303-5+A1:2023-05 p.5.6.3 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)
PN-EN 303-5:2021-09 p.5.7.6
PN-EN 303-5:2021-09 p.5.7.7 PN-EN 303-5+A1:2023-05 p.5.7.7 wskazane w Rozporządzeniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.) PN-EN 15456:2008
PN-EN 303-5:2021-09 p.5.9.4 PN-EN 303-5+A1:2023-05 p.5.9.4
PN-EN ISO 16994:2016-10
PN-EN ISO 17831-1:2016-02
PN-EN ISO 18134-2:2017-03 PN-EN ISO 18134-1:2023-02
PN-EN ISO 18135:2017-06 pkt 8
PN-EN ISO 21644:2021-07 pkt. B7
PN-EN ISO 21654-2021-12
PN-EN ISO 21656:2021-08
PN-EN ISO 21660-3:2021-08
PN-EN ISO 21663:2021-06
PN-EN ISO 22167:2021-08
PN-EN ISO 6976:2016-11
PN-G-04502:2014-11 pkt. 5.3.1.2.
PN-G-04502:2014-11 pkt.10
PN-G-04508:2020-05
PN-G-04511:1980 pkt. 2.3.2
PN-G-04512:1980/Az1:2002
PN-G-04516:1998 ISO 562:2024-08
PN-G-04534:2024-01
PN-G-04560:1998
PN-G-04571:1998 ISO 29541:2025-02
PN-G-04584:2001
PN-G-04611:2020-06
PN-G-04611:2020-06 pkt. 4.3.2
PN-G-04611:2020-06 pkt.4.4.5
PN-ISO 10396:2001
PN-ISO 11722:2009
PN-ISO 13909-7:2005
PN-ISO 13909-8:2005
PN-ISO 540:2001 (ISO 540:1995 IDT)
PN-ISO 579:2002
PN-ISO 589:2006 Metoda B1
PN-ISO 687:2005
PN-ISO 7404-3:2001
PN-ISO 7404-5:2002
PN-Z-04030-7:1994
Procedura Q/LCA/05/B:2022 PN-EN ISO 18134-3:2023-12
Procedura Q/LCA/06/B:2022 PN-EN ISO 18122:2023-05
Procedura Q/LCA/07/B:2022 PN-EN ISO 18123:2023-10
Procedura Q/LCA/08/B:2022
Procedura Q/LCA/09/B:2022 PN-EN ISO 16948:2015-07
Procedura Q/LCA/10/B:2022
Procedura Q/LCA/12/B:2022 PN-EN ISO 18125:2017-07
Procedura Q/LCA/16/B:2022
Procedura Q/LCA/24/B:2022
Procedura Q/LCA/26/B:2022
Procedura Q/LCA/27/B:2022 PN-EN ISO 18122:2023-05
Procedura Q/LCA/27/B:2022 PN-EN ISO 18134-3:2023-12
Procedura Q/LCA/32/B:2022
Procedura Q/LCA/33/B:2022
Procedura Q/LCA/44/B:2022
Procedura Q/LCA/53/B:2022
Procedura Q/LCA/54/B:2022
Procedura Q/LCA/55/B:2022
Procedura Q/LCA/56/B:2022
Procedura Q/LCA/57/B:2022
Procedura Q/LCA/58/B:2022
Procedura Q/LCA/60/B:2022
Procedura Q/LCA/62/B:2022
Procedura Q/LCA/63/B:2022
Procedura Q/LCA/65/B:2022
Procedura Q/LS/01/H:2023
Procedura Q/LS/02/H:2023
Procedura Q/LS/07/F:2023
Zharmonizowane specyfikacje techniczne
eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017 r. (Dz.U. 2017 poz. 1690 z późn.zm.)
eniu Ministra Rozwoju I Finansów z dnia 1 sierpnia 2017r. (Dz.U. 2017 poz. 1690 z późn.zm.)