National Technical Regulation QCVN 19:2024/BTNMT for Industrial emission
NATIONAL TECHNICAL REGULATION ON INDUSTRIAL EMISSION
Foreword
The QCVN 19:2024/BTNMT is compiled by the Pollution Control Department, submitted by Department of Science and Technology; appraised by the Ministry of Science and Technology, and promulgated by the Minister of Natural Resources and Environment under Circular No. ……/2024/TT-BTNMT dated …………………, 2024.
The QCVN 19:2024/BTNMT replaces:
QCVN 19:2009/BTNMT - National Technical Regulations on industrial emission for dust and inorganic substances;
QCVN 20:2009/BTNMT - National Technical Regulations on industrial emission for organic substances;
QCVN 21:2009/BTNMT - National Technical Regulations on industrial emission in chemical fertilizer production industry;
QCVN 22:2009/BTNMT - National Technical Regulations on industrial emission in thermal electricity industry;
QCVN 23:2009/BTNMT - National Technical Regulations on industrial emission in cement production industry;
QCVN 34:2010/BTNMT - National Technical Regulations on industrial emission in refinery and petrochemistry industry for dust and inorganic substances;
QCVN 51:2017/BTNMT - National Technical Regulations on industrial emission in steel production industry.
Limit values of pollutants under Schedule 1, Schedule 2 of the QCVN 19:2024/BTNMT replace upper limit of pollution parameters in emission:
Schedule 1 and Schedule 4 QCVN 41:2011/BTNMT - National Technical Regulations on co-processing of hazardous waste in cement kiln;
Schedule 2 QCVN 02:2012/BTNMT, National Technical Regulation on solid health care waste incinerator;
Schedule 2 QCVN 30:2012/BTNMT - National Technical Regulation on Industrial Waste Incinerator;
Schedule 4 QCVN 56:2013/BTNMT - National Technical Regulation on waste oil recycling;
Schedule 2 QCVN 61-MT:2016/BTNMT - National Technical Regulation on municipal solid waste incinerators.
NATIONAL TECHNICAL REGULATION ON INDUSTRIAL EMISSION
1. GENERAL PROVISIONS
1.1. Scope
1.1.1. This document prescribes limit values of pollution parameters in industrial emission discharged to the environment.
1.1.2. This document does not apply to emission discharge of transport vehicles.
1.2. Regulated entities
This document applies to environment state authorities; organizations, individuals related to discharge of industrial emission to the environment.
1.3. Definitions
In this Regulation, the terms below are construed as follows:
1.3.1. Industrial emission means a combination of particles and gases produced during production, business, service process.
1.3.2. Gas means materials in gas form produced as a result of combustion, synthesis, and decomposition of materials or as a result of physical properties of materials.
1.3.3. Particle means fine materials in solid or liquid form produced as a result of milling, classification, consolidation, mixing, physical preparation, combustion, synthesis, or decomposition of materials.
1.3.4. Particulate matter means particles suspended in or falling through the air.
1.3.5. Industrial emission discharge outlet (hereinafter referred to as “discharge outlet”) means an industrial emission source, including: structures, machinery, equipment, or equivalent items that discharge industrial emission via smokestacks or exhaust pipes.
1.3.6. Industrial emission discharge facility (hereinafter referred to as “discharge facility”) means an investment project, manufacturing facility, business establishment, or service establishment outfitted with a discharge outlet or discharge outlets.
1.3.7. Fuel means (solid, liquid, gaseous) materials used directly or in processed form for combustion.
1.3.8. Solid biomass means fuel of agricultural or forestry origin, including: cultivation by-products, by-products of natural wood processing, manufacturing processes that utilize natural wood, bamboo, used natural wood products that do not contain excessively hazardous waste in accordance with waste management laws (e.g. straw, husk, woodchips, sawdust, wood flour, wood pellets, coconut shells, cashew bagasse, roots, husk of crops and similar by-products).
1.3.9. Biogas means a gas mixture created from decomposition of organic substances initiated by bacteria in anaerobic environment.
1.3.4. Normal cubic meter of emission (Nm3) means a cubic meter of emission at 25 oC and atmospheric pressure of 760 mm of mercury.
1.3.11. Reference oxygen concentration (%) in industrial emission means a standard oxygen concentration defined during combustion of fuel in various forms at standard conditions.
1.3.12. Capacity of discharge outlet means the total capacity of discharge outlets of the same type and using the same fuel in a discharge facility.
1.3.13. Column A, Column B, and Column C in Schedule 1 and Schedule 2 are prescribed as follows:
1.3.13.1. Column A dictates limit values of pollution parameters in industrial emission produced by a discharge facility located in strictly protected areas.
1.3.13.2. Column B dictates limit values of pollution parameters in industrial emission produced by a discharge facility located in emission control area.
1.3.13.3. Column C dictates limit values of pollution parameters in industrial emission produced by a discharge facility located in area other than those specified under Section 1.3.13.1 and Section 1.3.13.2 hereof.
2. TECHNICAL PROVISIONS
2.1. Limit values of pollution parameters for “gases” in industrial emission discharged to the environment
On the basis of environment area classification under Section 1.3.13 hereof, limit values of pollution parameters for “gases” in industrial emission discharged to the environment are provided under Schedule 1:
Schedule 1. Limit values of pollution parameters for "gases”
|
No. |
Pollution parameter |
Unit |
Discharge outlet |
A |
B |
C |
|
1. |
Ammonia (NH3) |
mg/Nm3 |
1. Equipment for manufacturing fertilizer and nitrogen compound |
≤ 15 |
≤ 25 |
≤ 30 |
|
2. Equipment for manufacturing dyes and inorganic pigments |
≤ 15 |
≤ 25 |
≤ 30 |
|||
|
3. Equipment and incinerators for waste |
≤ 15 (12) |
≤ 20 (12) |
≤ 25 (12) |
|||
|
4. Clinker furnace in cement production (including co-processing of waste) |
≤ 15 (13) |
≤ 25 (13) |
≤ 30 (13) |
|||
|
5. Coke furnace in coke production |
≤ 15 (7) |
≤ 20 (7) |
≤ 25 (7) |
|||
|
6. Selective catalytic reduction (SCR) or selective non-catalytic reduction (SNCR) of discharge outlets other than the 5 aforementioned outlets |
≤ 15 |
≤ 20 |
≤ 25 |
|||
|
7. Other discharge outlets |
≤ 15 |
≤ 20 |
≤ 25 |
|||
|
2. |
Carbon monoxide (CO) |
mg/Nm3 |
1. Thermal fluid heater, industrial boiler (excluding waste incinerators) |
|
|
|
|
1.1. Equipment using liquid fuel |
|
|
|
|||
|
1.1.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 200 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
1.1.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 250 (4) |
≤ 350 (4) |
≤ 400 (4) |
|||
|
1.2. Equipment using solid fuel |
|
|
|
|||
|
1.2.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 250 (6) |
≤ 350 (6) |
≤ 400 (6) |
|||
|
1.2.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 300 (6) |
≤ 400 (6) |
≤ 450 (6) |
|||
|
1.3. Equipment using solid biomass |
≤ 200 (6) |
≤ 300 (6) |
≤ 350 (6) |
|||
|
1.4. Equipment using gaseous fuel |
≤ 80 (4) |
≤ 100 (4) |
≤ 120 (4) |
|||
|
2. Equipment and incinerators for waste |
|
|
|
|||
|
2.1. Incinerators having capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 120 (12) |
≤ 180 (12) |
≤ 200 (12) |
|||
|
2.2. Incinerators having capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 150 (12) |
≤ 200 (12) |
≤ 250 (12) |
|||
|
3. CO incinerators in refined petroleum products (refinery, petrochemistry) |
≤ 250 (12) |
≤ 300 (12) |
≤ 350 (12) |
|||
|
4. Equipment for producing and forging iron, steel, cast iron; non-ferrous metal; pre-cast metal (except sintering) |
|
|
|
|||
|
4.1. Blast furnace (BF) |
≤ 130 (7) |
≤ 180 (7) |
≤ 230 (7) |
|||
|
4.2. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace, reheating furnace, melting furnace |
≤ 130 |
≤ 180 |
≤ 230 |
|||
|
5. Furnace (including reheating furnace, drying oven) in production of cements, lime, gypsum, products thereof; Furnace (including reheating furnace, drying oven, melting furnace) in production of other non-metallic ore |
≤ 150 (13) |
≤ 250 (13) |
≤ 300 (13) |
|||
|
6. Coke furnace in coke production |
≤ 130 (7) |
≤ 180 (7) |
≤ 230 (7) |
|||
|
7. Cremator |
≤ 250 (12) |
≤ 300 (12) |
≤ 350 (12) |
|||
|
8. Other equipment using solid biomass |
≤ 200 (6) |
≤ 300 (6) |
≤ 350 (6) |
|||
|
9. Other discharge outlets |
≤ 300 |
≤ 400 |
≤ 450 |
|||
|
3. |
Hydrochloric acid (HCl) |
mg/Nm3 |
1. Equipment for manufacturing and recycling hydrochloric acid (including equipment for capturing hydrochloric acid and hypochlorite) |
≤ 6 |
≤ 8 |
≤ 10 |
|
2. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
2.1. Sintering furnace, sintering device |
≤ 4 (15) |
≤ 5 (15) |
≤ 7 (15) |
|||
|
2.2. Blast furnace (BF) |
≤ 4 (7) |
≤ 5 (7) |
≤ 7 (7) |
|||
|
2.3. Equipment for removing grease, treating surface |
≤ 4 |
≤ 5 |
≤ 7 |
|||
|
3. Equipment and incinerators for waste |
|
|
|
|||
|
3.1. Incinerators having capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 20 (12) |
≤ 25 (12) |
≤ 30 (12) |
|||
|
3.2. Incinerators having capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 25 (12) |
≤ 30 (12) |
≤ 35 (12) |
|||
|
4. Furnace, melting furnace in glass production and glass product manufacturing (in respect of glass fiber, pure oxygen is used instead of reference oxygen) |
≤ 3 (13) |
≤ 4 (13) |
≤ 5 (13) |
|||
|
5. Furnace in production of cement, lime, gypsum, and products thereof; furnace, melting furnace in production of other non-metal minerals |
≤ 15 (13) |
≤ 20 (13) |
≤ 25 (13) |
|||
|
6. Equipment for condensation, acid etching, surface treatment in production of superconductor and electronic components |
≤ 6 |
≤ 8 |
≤ 10 |
|||
|
7. Coke furnace in coke production |
≤ 4 (7) |
≤ 5 (7) |
≤ 7 (7) |
|||
|
8. Cremator |
≤ 30 (12) |
≤ 30 (12) |
≤ 30 (12) |
|||
|
9. Other discharge outlets |
≤ 10 |
≤ 15 |
≤ 20 |
|||
|
4. |
Sulfur dioxide (SO2) |
mg/Nm3 |
1. Thermal fluid heater, industrial boiler (excluding waste incinerators) |
|
|
|
|
1.1. Equipment using liquid fuel |
|
|
|
|||
|
1.1.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 200 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
1.1.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 250 (4) |
≤ 350 (4) |
≤ 400 (4) |
|||
|
1.2. Equipment using solid fuel |
|
|
|
|||
|
1.2.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 200 (6) |
≤ 300 (6) |
≤ 350 (6) |
|||
|
1.2.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 250 (6) |
≤ 350 (6) |
≤ 400 (6) |
|||
|
1.3. Equipment using solid biomass |
≤ 130 (6) |
≤ 200 (6) |
≤ 250 (6) |
|||
|
1.4. Equipment using gaseous fuel |
≤ 90 (4) |
≤ 120 (4) |
≤ 150 (4) |
|||
|
1.5. Equipment using biogas |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
2. Equipment in factories and power generation facilities |
|
|
|
|||
|
2.1. Equipment using liquid fuel (of capacity of 1 MW or higher) |
|
|
|
|||
|
2.1.1. Internal combustion engines and air turbines for power generation |
≤ 120 (15) |
≤ 200 (15) |
≤ 250 (15) |
|||
|
2.1.2. Other power generation equipment |
≤ 120 (4) |
≤ 200 (4) |
≤ 250 (4) |
|||
|
2.2. Equipment using solid fuel |
|
|
|
|||
|
2.2.1. Total capacities exceeding 1.200 MW |
≤ 120 (6) |
≤ 180 (6) |
≤ 200 (6) |
|||
|
2.2.2. Total capacities exceeding 300 MW to 1.200 MW |
≤ 120 (6) |
≤ 220 (6) |
≤ 250 (6) |
|||
|
2.2.3. Total capacities of 300 MW or lower |
≤ 120 (6) |
≤ 250 (6) |
≤ 300 (6) |
|||
|
2.3. Equipment using solid biomass |
≤ 130 (6) |
≤ 200 (6) |
≤ 250 (6) |
|||
|
2.4. Equipment using gaseous fuel |
|
|
|
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 1.200 MW |
≤ 50 (15) |
≤ 60 (15) |
≤ 70 (15) |
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 300 MW to 1.200 MW |
≤ 50 (15) |
≤ 70 (15) |
≤ 80 (15) |
|||
|
2.4.3. Combustion engine and air turbine for power generation having total capacities of 300 MW or lower |
≤ 50 (15) |
≤ 80 (15) |
≤ 90 (15) |
|||
|
2.4.4. Equipment using gas captured from coke furnace in coke production, carbon black production, and other production |
≤ 180 (6) |
≤ 200 (6) |
≤ 250 (6) |
|||
|
2.4.5. Equipment using biogas |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
2.4.6. Other power generation equipment |
≤ 100 (4) |
≤ 120 (4) |
≤ 150 (4) |
|||
|
3. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
3.1. Sintering furnace, sintering device |
≤ 150 (15) |
≤ 250 (15) |
≤ 300 (15) |
|||
|
3.2. Blast furnace (BF) |
≤ 150 (7) |
≤ 250 (7) |
≤ 300 (7) |
|||
|
3.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace, reheating furnace, melting furnace |
≤ 150 |
≤ 250 |
≤ 300 |
|||
|
4. Equipment for producing sulfuric acid in production of simple inorganic substances |
≤ 300 (8) |
≤ 350 (8) |
≤ 400 (8) |
|||
|
5. Equipment for mixing, reacting, refining, concentrating, heating in production of fertilizer and nitrogen compounds |
≤ 250 |
≤ 300 |
≤ 350 |
|||
|
6. Equipment for producing refined petroleum products (refinery, petrochemistry) |
|
|
|
|||
|
6.1. Equipment for gas flaring |
≤ 200 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
6.2. Equipment for reheating |
≤ 200 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
6.3. Equipment for CO combustion |
≤ 200 (12) |
≤ 250 (12) |
≤ 300 (12) |
|||
|
7. Equipment for reheating in production of simply organic substances |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
8. Equipment for producing coal gasification fuel |
|
|
|
|||
|
8.1. Equipment for drying |
≤ 100 (8) |
≤ 150 (8) |
≤ 200 (8) |
|||
|
8.2. Equipment for incineration |
≤ 200 (7) |
≤ 250 (7) |
≤ 350 (7) |
|||
|
8.3. Equipment for capturing sulfur |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
8.4. Equipment for producing sulfuric acid |
≤ 250 (8) |
≤ 300 (8) |
≤ 350 (8) |
|||
|
9. Coke furnace in coke production |
≤ 200 (7) |
≤ 250 (7) |
≤ 300 (7) |
|||
|
10. Equipment and incinerators for waste |
|
|
|
|||
|
10.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 80 (12) |
≤ 100 (12) |
≤ 150 (12) |
|||
|
10.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 100 (12) |
≤ 120 (12) |
≤ 180 (12) |
|||
|
11. Furnace, dying oven, reheating furnace in production of cement and cement products |
≤ 80 (13) |
≤ 100 (13) |
≤ 120 (13) |
|||
|
12. Furnace, dying oven, reheating furnace in production of lime, gypsum, products of lime and gypsum; ceramic and products thereof |
≤ 80 (13) |
≤ 100 (13) |
≤ 130 (13) |
|||
|
13. Furnace, melting furnace in glass production and glass product manufacturing (in respect of glass fiber, pure oxygen is used instead of reference oxygen) |
≤ 250 (13) |
≤ 300 (13) |
≤ 350 (13) |
|||
|
14. Cremator |
≤ 150 (12) |
≤ 200 (12) |
≤ 250 (12) |
|||
|
15. Other equipment using solid biomass |
≤ 200 (6) |
≤ 250 (6) |
≤ 300 (6) |
|||
|
16. Other discharge outlets |
≤ 200 |
≤ 300 |
≤ 350 |
|||
|
5. |
Nitrous oxide (NOx by NO2) |
mg/Nm3 |
1. Thermal fluid heater, industrial boiler (excluding waste incinerators) |
|
|
|
|
1.1. Equipment using liquid fuel |
|
|
|
|||
|
1.1.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 200 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
1.1.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 250 (4) |
≤ 400 (4) |
≤ 450 (4) |
|||
|
1.2. Equipment using solid fuel |
|
|
|
|||
|
1.2.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 200 (6) |
≤ 300 (6) |
≤ 350 (6) |
|||
|
1.2.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 250 (6) |
≤ 400 (6) |
≤ 450 (6) |
|||
|
1.3. Equipment using solid biomass |
≤ 150 (6) |
≤ 250 (6) |
≤ 300 (6) |
|||
|
1.4. Equipment using gaseous fuel |
≤ 70 (4) |
≤ 120 (4) |
≤ 150 (4) |
|||
|
1.5. Equipment using biogas |
≤ 150 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
2. Equipment in factories and power generation facilities |
|
|
|
|||
|
2.1. Equipment using liquid fuel (of capacity of 1 MW or higher) |
|
|
|
|||
|
2.1.2. Internal combustion engines and air turbines for power generation |
≤ 150 (15) |
≤ 250 (15) |
≤ 300 (15) |
|||
|
2.1.2. Other power generation equipment |
≤ 150 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
2.2. Equipment using solid fuel |
|
|
|
|||
|
2.2.1. Total capacities exceeding 1.200 MW |
≤ 120 (6) |
≤ 180 (6) |
≤ 200 (6) |
|||
|
2.2.2. Total capacities exceeding 300 MW to 1.200 MW |
≤ 120 (6) |
≤ 220 (6) |
≤ 250 (6) |
|||
|
2.2.3. Total capacities of 300 MW or lower |
≤ 120 (6) |
≤ 250 (6) |
≤ 300 (6) |
|||
|
2.3. Equipment using solid biomass |
≤ 150 (6) |
≤ 250 (6) |
≤ 300 (6) |
|||
|
2.4. Equipment using gaseous fuel |
|
|
|
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 1.200 MW |
≤ 50 (15) |
≤ 70 (15) |
≤ 90 (15) |
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 300 MW to 1.200 MW |
≤ 50 (15) |
≤ 90 (15) |
≤ 110 (15) |
|||
|
2.4.3. Combustion engine and air turbine for power generation having total capacities of 300 MW or lower |
≤ 70 (15) |
≤ 120 (15) |
≤ 150 (15) |
|||
|
2.4.4. Equipment using gas captured from coke furnace in coke production, carbon black production, and other production |
≤ 180 (6) |
≤ 200 (6) |
≤ 250 (6) |
|||
|
2.4.5. Lean-burn engine not using biogas |
≤ 80 (15) |
≤ 100 (15) |
≤ 150 (15) |
|||
|
2.4.6. Lean-burn engine using biogas |
≤ 180 (15) |
≤ 200 (15) |
≤ 250 (15) |
|||
|
2.4.7. Equipment using biogas |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
2.4.8. Other power generation equipment |
≤ 70 (4) |
≤ 120 (4) |
≤ 150 (4) |
|||
|
3. Equipment and incinerators for waste |
|
|
|
|||
|
3.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 180 (12) |
≤ 250 (12) |
≤ 300 (12) |
|||
|
3.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 200 (12) |
≤ 300 (12) |
≤ 350 (12) |
|||
|
4. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
4.1. Sintering furnace, sintering device |
≤ 150 (15) |
≤ 250 (15) |
≤ 300 (15) |
|||
|
4.2. Blast furnace (BF) |
≤ 150 (7) |
≤ 250 (7) |
≤ 300 (7) |
|||
|
4.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace, reheating furnace, melting furnace |
≤ 150 |
≤ 250 |
≤ 300 |
|||
|
5. Equipment for producing refined petroleum products (refinery, petrochemistry) |
|
|
|
|||
|
5.1. Equipment for reheating |
≤ 150 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
5.2. Equipment for CO combustion |
≤ 150 (12) |
≤ 200 (12) |
≤ 250 (12) |
|||
|
6. Equipment for production of simple organic substances |
|
|
|
|||
|
6.1. Reheating equipment using liquid, gas fuel |
≤ 150 (4) |
≤ 250 (4) |
≤ 300 (4) |
|||
|
6.2. Equipment for CO combustion |
≤ 150 (12) |
≤ 200 (12) |
≤ 250 (12) |
|||
|
7. Furnace, melting furnace in glass production and glass product manufacturing (in respect of glass fiber, pure oxygen is used instead of reference oxygen) |
≤ 200 (13) |
≤ 300 (13) |
≤ 350 (13) |
|||
|
8. Furnace, dying oven, reheating furnace in production of cement and cement products |
≤ 200 (13) |
≤ 350 (13) |
≤ 400 (13) |
|||
|
9. Furnace, dying oven, reheating furnace in production of lime, gypsum, products of lime and gypsum; ceramic and products thereof |
≤ 200 (13) |
≤ 350 (13) |
≤ 400 (13) |
|||
|
10. Equipment for producing coal gasification fuel |
|
|
|
|||
|
10.1. Equipment for drying |
≤ 200 (8) |
≤ 250 (8) |
≤ 300 (8) |
|||
|
10.2. Equipment for incineration |
≤ 200 (7) |
≤ 300 (7) |
≤ 350 (7) |
|||
|
10.3. Equipment for capturing sulfur |
≤ 250 (4) |
≤ 300 (4) |
≤ 350 (4) |
|||
|
10.4. Equipment for producing sulfuric acid |
≤ 200 (8) |
≤ 300 (8) |
≤ 350 (8) |
|||
|
11. Coke furnace in coke production |
≤ 200 (7) |
≤ 250 (7) |
≤ 300 (7) |
|||
|
12. Cremator |
≤ 200 (12) |
≤ 250 (12) |
≤ 300 (12) |
|||
|
13. Other equipment using solid biomass |
≤ 200 (6) |
≤ 300 (6) |
≤ 350 (6) |
|||
|
14. Re-heating equipment in production of fertilizer and inorganic substances |
≤ 250 |
≤ 400 |
≤ 450 |
|||
|
15. Other discharge outlets |
≤ 250 |
≤ 400 |
≤ 500 |
|||
|
6. |
Hydrogen sulfide (H2S) |
mg/Nm3 |
1. Equipment and incinerators for waste |
|
|
|
|
1.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 3 (12) |
≤ 3 (12) |
≤ 4 (12) |
|||
|
1.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 3 (12) |
≤ 4 (12) |
≤ 5 (12) |
|||
|
2. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 3 (13) |
≤ 5 (13) |
≤ 8 (13) |
|||
|
3. Reheating equipment, equipment for processing sulfur dioxide (SO2), gas flaring equipment in production of refined petroleum products (refinery, petrochemistry); production of simple organic substances |
≤ 4 (4) |
≤ 5 (4) |
≤ 6 (4) |
|||
|
4. Equipment for producing coal gasification fuel |
|
|
|
|||
|
4.1. Equipment for recovering sulfur |
≤ 4 (4) |
≤ 6 (4) |
≤ 8 (4) |
|||
|
4.2. Equipment for producing sulfuric acid |
≤ 4 (8) |
≤ 6 (8) |
≤ 8 (8) |
|||
|
5. Coke furnace in coke production |
≤ 2 (7) |
≤ 2,5 (7) |
≤ 3,0 (7) |
|||
|
6. Other discharge outlets |
≤ 6 |
≤ 7 |
≤ 8 |
|||
|
7. |
Fluorine (F) and F compounds (by fluoride) |
mg/Nm3 |
1. Equipment for melting in production of ceramics and products thereof |
≤ 2 (13) |
≤ 3 (13) |
≤ 3 (13) |
|
2. Equipment for wet sulfuric acid process, production of mixed fertilizer, production of ammonium superphosphate; equipment for melting phosphate or fluoride, equipment for production of fluorine compounds in production of simple organic substances; production of chemical fertilizer and nitrogen compound |
≤ 2 |
≤ 3 |
≤ 3 |
|||
|
3. Equipment and incinerators for waste |
|
|
|
|||
|
3.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 2 (12) |
≤ 3 (12) |
≤ 4 (12) |
|||
|
3.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 3 (12) |
≤ 4 (12) |
≤ 5 (12) |
|||
|
4. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 2 (13) |
≤ 3 (13) |
≤ 4 (13) |
|||
|
5. Equipment for surface treatment (including equipment for condensation and acid etching) in production of metal products, superconductor; electronic parts |
≤ 3 |
≤ 3 |
≤ 4 |
|||
|
6. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
6.1. Sintering furnace, sintering device |
≤ 4 (15) |
≤ 6 (15) |
≤ 7 (15) |
|||
|
6.2. Blast furnace (BF) |
≤ 4 (7) |
≤ 6 (7) |
≤ 7 (7) |
|||
|
6.3. Equipment for removing grease, treating surface |
≤ 3 |
≤ 3 |
≤ 4 |
|||
|
7. Coke furnace in coke production |
≤ 2 (13) |
≤ 3 (7) |
≤ 4 (7) |
|||
|
8. Other discharge outlets |
≤ 2 |
≤ 3 |
≤ 4 |
|||
|
8. |
Mercury (Hg) and Hg compounds (by Hg) |
mg/Nm3 |
1. Equipment and incinerators for waste |
≤ 0,05 (12) |
≤ 0,05 (12) |
≤ 0,08 (12) |
|
2. Power generator using solid fuel (power plant, power generation facility) |
≤ 0,04 (6) |
≤ 0,04 (6) |
≤ 0,05 (6) |
|||
|
3. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
3.1. Sintering furnace, sintering device |
≤ 0,04 (15) |
≤ 0,04 (15) |
≤ 0,05 (15) |
|||
|
3.2. Blast furnace (BF) |
≤ 0,04 (7) |
≤ 0,04 (7) |
≤ 0,05 (7) |
|||
|
3.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF) |
≤ 0,04 |
≤ 0,04 |
≤ 0,05 |
|||
|
4. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 0,04 (13) |
≤ 0,05 (13) |
≤ 0,08 (13) |
|||
|
5. Coke furnace in coke production |
≤ 0,04 (7) |
≤ 0,04 (7) |
≤ 0,05 (7) |
|||
|
6. Other discharge outlets |
≤ 0,05 |
≤ 0,1 |
≤ 0,1 |
|||
|
9. |
Volatile organic compounds (by TVOC, including constituents of: benzene, toluene, ethylbenzene, xylene, ethyl acetate, butyl acetate) |
mg/Nm3 |
1. Equipment for painting, surface coating (including equipment for drying, applying spray paint, applying mastic paint, applying dip paint) |
≤ 50 |
≤ 80 |
≤ 100 |
|
2. Equipment for printing |
≤ 50 |
≤ 80 |
≤ 100 |
|||
|
3. Equipment for manufacturing paint, varnish, similar paint and surface substances; manufacturing printing ink and mastics; adhesive |
≤ 80 |
≤ 120 |
≤ 150 |
|||
|
4. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 30 (13) |
≤ 30 (13) |
≤ 40 (13) |
|||
|
5. Equipment for removing grease, treating surface |
≤ 50 |
≤ 80 |
≤ 100 |
|||
|
6. Equipment and incinerators for waste |
≤ 30 (12) |
≤ 40 (12) |
≤ 50 (12) |
|||
|
7. Equipment in manufacturing of natural or synthetic rubber |
≤ 80 |
≤ 100 |
≤ 150 |
|||
|
8. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
8.1. Sintering furnace, sintering device |
≤ 10 (15) |
≤ 12 (15) |
≤ 15 (15) |
|||
|
8.2. Blast furnace (BF) |
≤ 10 (7) |
≤ 12 (7) |
≤ 15 (7) |
|||
|
8.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF) |
≤ 10 |
≤ 12 |
≤ 15 |
|||
|
9. Coke furnace in coke production |
≤ 10 (7) |
≤ 12 (7) |
≤ 15 (7) |
|||
|
10. Other discharge outlet (excluding internal combustion engines using natural gas) |
≤ 80 |
≤ 120 |
≤ 150 |
|||
|
10. |
Dioxins/Furans |
ngTEQ/ Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 0,05 (15) |
≤ 0,1 (15) |
≤ 0,2 (15) |
|||
|
1.2. Electric arc furnace (EAF), electric induction furnace |
≤ 0,05 |
≤ 0,1 |
≤ 0,2 |
|||
|
2. Furnace, melting furnace in production of aluminum and products therefrom |
≤ 0,05 |
≤ 0,3 |
≤ 0,4 |
|||
|
3. Furnace, melting furnace in production of copper and products therefrom |
≤ 0,05 |
≤ 0,3 |
≤ 0,4 |
|||
|
4. Furnace, melting furnace in production of zinc and zinc recovery |
≤ 0,05 |
≤ 0,3 |
≤ 0,4 |
|||
|
5. Equipment and incinerators for waste |
|
|
|
|||
|
5.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 0,2 (12) |
≤ 0,2 (12) |
≤ 0,3 (12) |
|||
|
5.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 0,3 (12) |
≤ 0,3 (12) |
≤ 0,4 (12) |
|||
|
6. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 0,2 (13) |
≤ 0,2 (13) |
≤ 0,3 (13) |
|||
|
7. Equipment for manufacturing refined petroleum products (refinery, petrochemistry) (production phase containing chloride such as: vinyl chloride, ethylene dichloride, etc.) |
≤ 0,05 |
≤ 0,08 |
≤ 0,1 |
|||
|
8. Other discharge outlets (specific equipment in waste treatment, waste co-treatment, or production model that may produce Dioxins/Furans) |
≤ 0,2 |
≤ 0,3 |
≤ 0,4 |
|||
|
11. |
Hydrogen cyanide (HCN) |
mg/Nm3 |
Equipment for incinerating exhaust in production of acrylonitrile; other discharge outlets |
≤ 8 |
≤ 9 |
≤ 10 |
|
12. |
Arsenic (As) and As compounds (by As) |
mg/Nm3 |
Other discharge outlets |
≤ 2 |
≤ 3 |
≤ 4 |
|
13. |
Chlorine (by Cl2) |
mg/Nm3 |
1.1. Equipment for manufacturing Chlorine |
≤ 4 |
≤ 6 |
≤ 8 |
|
1.2. Other discharge outlets |
≤ 4 |
≤ 5 |
≤ 6 |
|||
|
14. |
H2SO4 vapor |
mg/Nm3 |
1.1. Equipment for producing sulfuric acid |
≤ 10 |
≤ 30 |
≤ 35 |
|
1.2. Other discharge outlets |
≤ 10 |
≤ 20 |
≤ 25 |
|||
|
15. |
Bromine (Br) and Br compounds (by Br2) |
mg/Nm3 |
Equipment for manufacturing, using chemicals containing Bromine; other discharge outlets |
≤ 10 |
≤ 10 |
≤ 15 |
|
16. |
Carbon disulfide (CS2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 30 |
≤ 35 |
≤ 40 |
|
17. |
Acrylonitrile (C3H3N) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 6 |
≤ 7 |
≤ 8 |
|
18. |
Acetaldehyde (CH3CHO) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 50 |
≤ 100 |
≤ 150 |
|
19. |
Aniline (C6H5NH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 10 |
≤ 15 |
≤ 18 |
|
20. |
Benzene (C6H6) |
mg/Nm3 |
Equipment for manufacturing organic substances (depending on type of products and chemicals used), manufacturing refined petroleum products (refinery, petrochemistry); other discharge outlets |
≤ 4 |
≤ 5 |
≤ 5 |
|
21. |
Benzyl chloride (C6H5CH2CI) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 4 |
≤ 5 |
≤ 5 |
|
22. |
1,3-Butadiene (C4H6) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 15 |
≤ 20 |
≤ 25 |
|
23. |
Butylamine (CH3(CH2)2CH2 NH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 10 |
≤ 15 |
≤ 15 |
|
24. |
Cresol (CH3C6H4OH) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 15 |
≤ 20 |
≤ 20 |
|
25. |
Chloroform (CHCI3) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 25 |
≤ 30 |
≤ 30 |
|
26. |
ß-chloroprene (CH2=CCICH= CH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 30 |
≤ 40 |
≤ 50 |
|
27. |
Diethylamine ((C2H5)2NH) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 30 |
≤ 40 |
≤ 50 |
|
28. |
Dichloromethane (CH2Cl2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 170 |
≤ 200 |
≤ 250 |
|
29. |
1,1-Dichloroethane (CHCI2CH3) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 50 |
≤ 60 |
≤ 80 |
|
30. |
1,2-Dichloroethane (CICH=CHCI) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 50 |
≤ 60 |
≤ 80 |
|
31. |
1,4-Dioxane (C4H8O2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 100 |
≤ 150 |
≤ 200 |
|
32. |
Dimethylaniline (C6H5N(CH3)2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 15 |
≤ 20 |
≤ 25 |
|
33. |
Dimethyl sulfate ((CH3)2SO4) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 0,3 |
≤ 0,4 |
≤ 0,5 |
|
34. |
Ethylamine (CH3CH2NH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 30 |
≤ 35 |
≤ 40 |
|
35. |
Ethylbenzene (CH3CH2C6H5) |
mg/Nm3 |
Equipment for manufacturing organic substances (depending on type of products and chemicals used), manufacturing refined petroleum products (refinery, petrochemistry), recycling plastics; other discharge outlets |
≤ 100 |
≤ 120 |
≤ 150 |
|
36. |
Ethyl acrylate (CH2=CHCOO C2H5) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 60 |
≤ 70 |
≤ 80 |
|
37. |
Ethylene oxide (CH2OCH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 10 |
≤ 15 |
≤ 15 |
|
38. |
Formaldehyde (HCHO) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 10 |
≤ 15 |
≤ 20 |
|
39. |
Methanethiol (CH3SH) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 10 |
≤ 12 |
≤ 15 |
|
40. |
Methyl acrylate (CH2=CHCOO CH3) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 20 |
≤ 30 |
≤ 35 |
|
41. |
Methanol (CH3OH) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 100 |
≤ 150 |
≤ 200 |
|
42. |
Methyl bromide (CH3Br) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 60 |
≤ 70 |
≤ 80 |
|
43. |
Methyl chloride (CH3CI) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 100 |
≤ 120 |
≤ 150 |
|
44. |
Nitrobenzene (C6H5NO2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 3 |
≤ 4 |
≤ 5 |
|
45. |
Phenol and phenol compounds (C6H5OH) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 15 |
≤ 15 |
≤ 15 |
|
46. |
Propylene oxide (C3H6O) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 30 |
≤ 40 |
≤ 50 |
|
47. |
Styrene (C6H5CH=CH2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 100 |
≤ 100 |
≤ 100 |
|
48. |
1,1,2,2- Tetrachloroethene (CI2HCCHCI2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 20 |
≤ 25 |
≤ 30 |
|
49. |
Tetrachloromethane (CCl4) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 20 |
≤ 30 |
≤ 40 |
|
50. |
Toluene (C6H5CH3) |
mg/Nm3 |
Equipment for manufacturing organic substances (depending on type of products and chemicals used), manufacturing refined petroleum products (refinery, petrochemistry), recycling plastics; other discharge outlets |
≤ 30 |
≤ 40 |
≤ 50 |
|
51. |
Trichloroethylene (CICH=CCI2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 80 |
≤ 90 |
≤ 100 |
|
52. |
1,1,2- Trichloroethane (CHCI2CH2CI) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used); other discharge outlets |
≤ 100 |
≤ 150 |
≤ 200 |
|
53. |
Xylene (C6H4(CH3)2) |
mg/Nm3 |
Equipment for manufacturing, using organic chemicals (depending on type of products and chemicals used), recycling plastics; other discharge outlets |
≤ 50 |
≤ 100 |
≤ 150 |
|
54. |
vinyl chloride (CH2=CHCI) |
mg/Nm3 |
1. Equipment for polymerization and copolymerization in production of ethylene dichloride, vinyl chloride, and polyvinyl chloride (PVC) |
≤ 20 |
≤ 20 |
≤ 20 |
|
2. Equipment for reheating and extruding in PVC product manufacturing |
≤ 20 |
≤ 20 |
≤ 20 |
|||
|
3. Other discharge outlets |
≤ 25 |
≤ 30 |
≤ 30 |
|||
|
Note: - Values contained in brackets “( )” in Column A, Column B, or Column C of this Schedule refer to reference oxygen concentration. - Values associated with Mercury and Dioxines/Furans under this Schedule include gases and particles. - Values of Dioxins/Furans are calculated in accordance with Appendix 2 hereof. |
||||||
2.2. Limit values of pollution parameters for “particles” in industrial emission discharged to the environment
On the basis of environment area classification under Section 1.3.13 hereof, limit values of pollution parameters for “particles ” in industrial emission discharged to the environment are provided under Schedule 2:
Schedule 2. Limit values of pollution parameters for "particles”
|
No. |
Pollution parameter |
Unit |
Discharge outlet |
A |
B |
C |
|
1 |
Particulate matter |
mg/Nm3 |
1. Thermal fluid heater, industrial boiler (excluding waste incinerators) |
|
|
|
|
1.1. Equipment using liquid fuel |
|
|
|
|||
|
1.1.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 30 (4) |
≤ 40 (4) |
≤ 50 (4) |
|||
|
1.1.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 30 (4) |
≤ 45 (4) |
≤ 55 (4) |
|||
|
1.2. Equipment using solid fuel |
|
|
|
|||
|
1.2.1. Equipment having boiler capacities of 20 tonne/hour or higher or calorific value of 12.380.000 Kcal/hour or higher |
≤ 30 (6) |
≤ 40 (6) |
≤ 50 (6) |
|||
|
1.2.2. Equipment having boiler capacities below 20 tonne/hour or calorific value below 12.380.000 Kcal/hour |
≤ 40 (6) |
≤ 50 (6) |
≤ 60 (6) |
|||
|
1.3. Equipment using solid biomass |
≤ 40 (6) |
≤ 50 (6) |
≤ 60 (6) |
|||
|
1.4. Equipment using gaseous fuel |
≤ 20 (4) |
≤ 20 (4) |
≤ 30 (4) |
|||
|
1.5. Equipment using biogas |
≤ 20 (4) |
≤ 25 (4) |
≤ 35 (4) |
|||
|
2. Equipment in factories and power generation facilities |
|
|
|
|||
|
2.1. Equipment using liquid fuel (of capacity of 1 MW or higher) |
|
|
|
|||
|
2.1.1. Internal combustion engines and air turbines for power generation |
≤ 20 (15) |
≤ 25 (15) |
≤ 30 (15) |
|||
|
2.1.2. Other power generation equipment |
≤ 20 (4) |
≤ 25 (4) |
≤ 30 (4) |
|||
|
2.2. Equipment using solid fuel |
|
|
|
|||
|
2.2.1. Total capacities exceeding 1.200 MW |
≤ 20 (6) |
≤ 30 (6) |
≤ 35 (6) |
|||
|
2.2.2. Total capacities exceeding 300 MW to 1.200 MW |
≤ 20 (6) |
≤ 30 (6) |
≤ 35 (6) |
|||
|
2.2.3. Total capacities of 300 MW or lower |
≤ 25 (6) |
≤ 35 (6) |
≤ 45 (6) |
|||
|
2.3. Equipment using solid biomass |
≤ 25 (6) |
≤ 40 (6) |
≤ 50 (6) |
|||
|
2.4. Equipment using gaseous fuel |
|
|
|
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 1.200 MW |
≤ 15 (15) |
≤ 15 (15) |
≤ 20 (15) |
|||
|
2.4.1. Combustion engine and air turbine for power generation having total capacities exceeding 300 MW to 1.200 MW |
≤ 15 (15) |
≤ 15 (15) |
≤ 20 (15) |
|||
|
2.4.3. Combustion engine and air turbine for power generation having total capacities of 300 MW or lower |
≤ 15 (15) |
≤ 15 (15) |
≤ 20 (15) |
|||
|
2.4.4. Equipment using gas captured from coke furnace in coke production, carbon black production, and other production |
≤ 20 (6) |
≤ 30 (6) |
≤ 40 (6) |
|||
|
2.4.5. Other power generation equipment |
≤ 20 (4) |
≤ 30 (4) |
≤ 40 (4) |
|||
|
3. Equipment and incinerators for waste |
|
|
|
|||
|
3.1. Equipment having incineration capacities of 2 tonne/hour or higher (or 0,2 tonne/hour or higher in case of biomedical waste incinerators) |
≤ 30 (12) |
≤ 40 (12) |
≤ 45 (12) |
|||
|
3.2. Equipment having incineration capacities below 2 tonne/hour (or below 0,2 tonne/hour in case of biomedical waste incinerators) |
≤ 35 (12) |
≤ 45 (12) |
≤ 50 (12) |
|||
|
4. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|||
|
4.1. Sintering furnace, sintering device |
≤ 20 (15) |
≤ 30 (15) |
≤ 35 (15) |
|||
|
4.2. Blast furnace (BF) |
≤ 20 (7) |
≤ 30 (7) |
≤ 35 (7) |
|||
|
Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace, forging equipment, and other equipment |
≤ 20 |
≤ 30 |
≤ 35 |
|||
|
5. Furnace and drying oven in production of chemical fertilizer and nitrogen compounds |
≤ 30 (7) |
≤ 40 (7) |
≤ 50 (7) |
|||
|
6. Equipment for manufacturing coke |
|
|
|
|||
|
6.1. Equipment for manufacturing coke |
|
|
|
|||
|
6.1.1. Coke furnace |
≤ 20 (7) |
≤ 30 (7) |
≤ 35 (7) |
|||
|
6.1.2. Other discharge outlets |
≤ 20 |
≤ 30 |
≤ 35 |
|||
|
6.2. Equipment for manufacturing petroleum coke |
|
|
|
|||
|
6.2.1. Equipment for incineration |
≤ 20 (4) |
≤ 30 (4) |
≤ 35 (4) |
|||
|
6.2.2. Other discharge outlets |
≤ 20 |
≤ 30 |
≤ 35 |
|||
|
7. Equipment for producing refined petroleum products (refinery, petrochemistry) and simple organic substances |
|
|
|
|||
|
7.1. Equipment for gas flaring |
≤ 20 (4) |
≤ 30 (4) |
≤ 35 (4) |
|||
|
7.2. Equipment for reheating and catalyst regeneration |
≤ 20 (4) |
≤ 30 (4) |
≤ 35 (4) |
|||
|
7.3. Equipment for CO combustion |
≤ 30 (12) |
≤ 30 (12) |
≤ 35 (12) |
|||
|
7.4. Other equipment for particulate matter treatment |
≤ 30 |
≤ 30 |
≤ 35 |
|||
|
8. Equipment for producing coal gasification fuel |
|
|
|
|||
|
8.1. Equipment for drying |
≤ 30 (8) |
≤ 40 (8) |
≤ 50 (8) |
|||
|
8.2. Equipment for incineration |
≤ 30 (7) |
≤ 40 (7) |
≤ 50 (7) |
|||
|
8.3. Equipment for recovering sulfur |
≤ 30 (4) |
≤ 40 (4) |
≤ 60 (4) |
|||
|
8.4. Equipment for producing sulfuric acid |
≤ 30 (8) |
≤ 40 (8) |
≤ 50 (8) |
|||
|
8.5. Other equipment for particulate matter treatment |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
9. Furnace, melting furnace in glass production and glass product manufacturing (in respect of glass fiber, pure oxygen is used instead of reference oxygen) |
|
|
|
|||
|
9.1. Continuous furnace or electric furnace (except open-hearth electric furnace or top-covered furnace) |
≤ 30 (13) |
≤ 40 (13) |
≤ 50 (13) |
|||
|
9.2. Other melting furnace |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
10. Equipment in production of ceramic and ceramic products |
≤ 30 (13) |
≤ 40 (13) |
≤ 50 (13) |
|||
|
10.1. Furnace, melting furnace |
≤ 30 (13) |
≤ 40 (13) |
≤ 50 (13) |
|||
|
10.2. Other equipment for particulate matter treatment |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
11. Equipment for producing cement, lime, gypsum, and products thereof |
|
|
|
|||
|
11.1. Clinker furnace, equipment for reheating, drying |
≤ 20 (13) |
≤ 25 (13) |
≤ 30 (13) |
|||
|
11.2. Equipment for milling, cooling, and other equipment |
≤ 20 |
≤ 35 |
≤ 40 |
|||
|
12. Equipment for producing asbestos, insulating cotton in production of products of non-metal minerals |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
13. Equipment for painting (applying spray paint, applying mastic paint, applying dip paint) and drying |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
14. Equipment for surface treatment (including equipment for condensation and acid etching) in production of superconductor, electronic parts |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
15. Equipment for treating metal surface |
≤ 30 |
≤ 40 |
≤ 50 |
|||
|
16. Cremator |
≤ 50 (12) |
≤ 60 (12) |
≤ 70 (12) |
|||
|
17. Other equipment using solid biomass |
≤ 40 (6) |
≤ 50 (6) |
≤ 60 (6) |
|||
|
18. Other discharge outlets |
≤ 50 |
≤ 80 |
≤ 100 |
|||
|
2 |
Lead (Pb) and Pb compounds (by Pb) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 0,9 (15) |
≤ 1,2 (15) |
≤ 1,5 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 0,9 (7) |
≤ 1,2 (7) |
≤ 1,5 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 0,9 |
≤ 1,2 |
≤ 1,5 |
|||
|
2. Coke furnace in coke production |
≤ 0,9 (7) |
≤ 1,2 (7) |
≤ 1,5 (7) |
|||
|
3. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 0,8 |
≤ 1 |
≤ 1 |
|||
|
3 |
Cadmium (Cd) and Cd compounds (by Cd) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 0,1 (15) |
≤ 0,15 (15) |
≤ 0,2 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 0,1 (7) |
≤ 0,15 (7) |
≤ 0,2 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 0,1 |
≤ 0,15 |
≤ 0,2 |
|||
|
2. Coke furnace in coke production |
≤ 0,1 (7) |
≤ 0,15 (7) |
≤ 0,2 (7) |
|||
|
3. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 0,2 |
≤ 0,2 |
≤ 0,2 |
|||
|
4 |
Chrome (Cr) and Cr compounds (by Cr) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 1 (15) |
≤ 2 (15) |
≤ 2,5 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 1 (7) |
≤ 2 (7) |
≤ 2,5 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), melting furnace |
≤ 1 |
≤ 2 |
≤ 2,5 |
|||
|
2. Coke furnace in coke production |
≤ 1 (7) |
≤ 2 (7) |
≤ 2,5 (7) |
|||
|
3. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 0,5 |
≤ 1 |
≤ 2 |
|||
|
5 |
Copper (Cu) and Cu compounds (by Cu) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 4 (15) |
≤ 5 (15) |
≤ 6 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 4 (7) |
≤ 5 (7) |
≤ 6 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 4 |
≤ 5 |
≤ 6 |
|||
|
2. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 4 |
≤ 5 |
≤ 6 |
|||
|
6 |
Nickel (Ni) and Ni compounds (by Ni) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 0,5 (15) |
≤ 1 (15) |
≤ 1,2 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 0,5 (7) |
≤ 1 (7) |
≤ 1,2 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 0,5 |
≤ 1 |
≤ 1,2 |
|||
|
2. Coke furnace in coke production |
≤ 0,5 (7) |
≤ 1 (7) |
≤ 1,2 (7) |
|||
|
3. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 1 |
≤ 2 |
≤ 2 |
|||
|
7 |
Zinc (Zn) and Zn compounds (by Zn) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 8 (15) |
≤ 10 (15) |
≤ 12 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 8 (7) |
≤ 10 (7) |
≤ 12 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 8 |
≤ 10 |
≤ 12 |
|||
|
2. Other discharge outlets |
≤ 6 |
≤ 7 |
≤ 8 |
|||
|
8 |
Antimony (Sb) and Sb compounds (by Sb) |
mg/Nm3 |
1. Equipment for manufacturing and forging iron, steel, cast iron, non-ferrous metal, and products of pre-cast metal |
|
|
|
|
1.1. Sintering furnace, sintering device |
≤ 5 (15) |
≤ 6 (15) |
≤ 8 (15) |
|||
|
1.2. Blast furnace (BF) |
≤ 5 (7) |
≤ 6 (7) |
≤ 8 (7) |
|||
|
1.3. Electric arc furnace (EAF), electric induction furnace, basic oxygen furnace (BOF), ladle furnace (LF), reheating furnace, melting furnace |
≤ 5 |
≤ 6 |
≤ 8 |
|||
|
2. Other discharge outlets (except for waste incineration and waste co-treatment by total metal) |
≤ 5 |
≤ 6 |
≤ 8 |
|||
|
9 |
Total metal Cd, Tl, and equivalent compounds |
mg/Nm3 |
1. Equipment and incinerators for waste |
≤ 0,05 (12) |
≤ 0,05 (12) |
≤ 0,05 (12) |
|
2. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 0,05 (13) |
≤ 0,05 (13) |
≤ 0,05 (13) |
|||
|
10 |
Total metal (including: Sb, As, Pb, Cr, Co, Cu, Mn, Ni, V and corresponding compounds) |
mg/Nm3 |
1. Equipment and incinerators for waste |
≤ 0,5 (12) |
≤ 0,5 (12) |
≤ 0,5 (12) |
|
2. Clinker furnace in cement production (only applicable in waste co-incineration) |
≤ 0,5 (13) |
≤ 0,5 (13) |
≤ 0,5 (13) |
|||
|
11 |
Polycyclic aromatic hydrocarbons - PAH (by equivalent Benzo[a]pyrene) |
mg/Nm3 |
1. Coke furnace in coke production |
≤ 0,05 (7) |
≤ 0,06 (7) |
≤ 0,08 (7) |
|
2. Other discharge outlets |
≤ 0,05 |
≤ 0,1 |
≤ 0,1 |
|||
|
12 |
Smoke opacity |
Ringelmann scale |
All discharge outlets |
≤ 2 |
≤ 2 |
≤ 2 |
|
Note: - Values contained in brackets “( )” in Column A, Column B, or Column C of this Schedule refer to reference oxygen concentration. - Values associated to Polycyclic aromatic hydrocarbons - PAH (by equivalent Benzo[a]pyrene) under Schedule 2 (including gases and particles) shall be calculated in accordance with Appendix 3 hereof. |
||||||
3. DETERMINATION METHODS
3.1. Methods for determining pollution parameters in industrial emissions (including on-site measurement and sampling, and laboratory assessment) shall conform to Appendix 1 hereof.
Where a pollution parameter can be determined via multiple measurement, sampling, test (analysis) methods and may require arbitration in case of disputes or complaints, the first method mentioned under Column 3 and Column 4 Appendix 1 hereof shall be adopted.
3.2. Approval for other measurement, sampling, test methods (that are not mentioned under Column 3 and Column 4 Appendix 1 hereof), including:
3.3. The use of measuring instruments under Column 3 Appendix 1 hereof must meet technical requirements pertaining to environmental monitoring as per the law.
4. REGULATIONS ON MANAGEMENT
4.1. Pollution parameters and limit values of pollution parameters of industrial emission of investment projects, discharge facilities must be specified under decision approving evaluation results of environmental impact assessment reports, environment permit, and environment registration.
4.2. Pollution parameters to be controlled of industrial emission discharge outlets in investment projects and discharge facilities must be specified under decision approving evaluation results of environmental impact assessment reports, environment permit, including:
4.2.1. Pollution parameters that have been specified by type of industrial emission discharge outlets are mentioned under Schedule 1 and Schedule 2 hereof.
4.2.2. Certain pollution parameter(s) under Schedule 1 and Schedule 2 have not been specified by type of industrial emission discharge outlets.
4.2.3. Several new characteristic pollution parameters that arise in investment projects or facilities via technology, equipment have not been specified in Schedule 1 and Schedule 2 hereof.
4.3. Where new characteristic pollution parameters found in investment projects or facilities are not specified under Schedule 1 and Schedule 2 hereof, limit values of corresponding pollution parameters under national standards on environmental protection of any countries among the G7 Group shall be adopted.
4.4. Where monitoring and analysis results of pollution parameters do not exceed limit values under Schedule 1 and Schedule 2 hereof (or limit values dictated under national standards on environmental protection of any countries among the G7 Group in case of new characteristic pollution parameters under Section 4.2.3 hereof), the discharge of industrial emission shall be deemed compliant and conform to this document.
4.5. Methods for assessing compliance and conformity with this document shall be carried out by monitoring and analyzing emission sample prior to discharge to the environment.
4.6. Monitoring and analysis of pollution parameters under Schedule 1 and Schedule 2 hereof for the purpose of providing state authorities with information and data shall be carried out by organizations to which certificate of eligibility to provide environmental monitoring service has been issued. Monitoring and analysis of new characteristic pollution parameters under Section 4.2.3 hereof shall be carried out by organizations to which certificate of registration for test operation has been issued in accordance with Decree No. 107/2016/ND-CP dated July 1, 2016 of the Government. The use of automatic and continuous emission monitoring results shall conform to regulations of the law.
4.7. Assessment results of compliance and conformity to this document shall act as the basis to enable state authorities to consider and take actions as per the law.
5. RESPONSIBILITIES OF ORGANIZATIONS AND INDIVIDUALS
5.1. Developers of investment projects and discharge facilities shall be responsible for maintaining pollution parameters below limit values under Schedule 1 and Schedule 2 hereof.
5.2. Developers of investment projects and discharge facilities shall be responsible for determining pollution parameters of industrial emission discharge outlets in accordance with Section 4.2 hereof on the basis of: Information on type of production, business, service; industrial emission discharge outlets; manufacturing technology, waste treatment technology; ingredients, materials, fuel, chemicals used, and list of pollution parameters that may occur (proposed under application for approval for environmental impact assessment report, application for issuance, renewal, and reissuance of environment permit).
5.3. Competent authorities appraising environmental impact assessment report and issuing environment permit shall determine pollution parameters to be controlled via proposition of developers of investment projects and discharge facilities under application for approval for environmental impact assessment report, application for issuance, renewal, and reissuance of environment permit. Where other pollution parameters exceed limit values under Schedule 1 and Schedule 2 hereof, additional control shall be required as per the law.
6. ORGANIZING IMPLEMENTATION
6.1. People's Committees of provinces are responsible for reviewing and amending technical regulations on local environment pertaining to industrial emission in order to stay in line with regulations of the law, local socio-economic development, and this document.
6.2. Environmental protection authorities shall be responsible for guiding, examining, and supervising implementation of this Regulation.
6.3. Where documents referred to hereunder are amended or superseded, the new documents shall prevail./.
Appendix 1
Methods for determining pollution parameters in industrial emission
|
No. |
Measurement reading, pollution parameter |
Test method and standard number |
|
|
On-site measurement and sampling |
Laboratory analysis |
||
|
(1) |
(2) |
(3) |
(4) |
|
1 |
Identification of sampling locations |
US EPA Method 1 US EPA Method 1A |
- |
|
2 |
Velocity and flow rate |
TCVN 11303:2016 TCVN 5977:2009 TCVN 120-29:2018 US EPA Method 2 ISO 10780 EPA Method 2A EPA Method 2C EPA Method 2D |
- |
|
3 |
Molecular weight of dry air |
TCVN 11304:2016 TCVN 5977:2009 US EPA Method 3 |
- |
|
4 |
Moisture content |
TCVN 11305:2016 TCVN 5977:2009 US EPA Method 4 Direct measuring instrument |
- |
|
5 |
Oxygen (O2) |
Direct measuring instrument |
- |
|
6 |
Temperature |
Direct measuring instrument |
- |
|
7 |
Pressure |
Direct measuring instrument |
- |
|
8 |
Ammonia (NH3) |
JIS K 0099:2020 |
JIS K 0099:2020 |
|
9 |
Carbon monoxide (CO) |
CEN/TS 17337:2019 US EPA Method 10 Direct measuring instrument |
- |
|
10 |
Hydrochloric acid (HCl) |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A TCVN 7244:2003 |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A TCVN 7244:2003 |
|
11 |
Sulfur dioxide (SO2) |
TCVN 11306:2016 TCVN 6750:2005 US EPA Method 6 US EPA Method 6C US EPA Method 8 US EPA Method 8A Direct measuring instrument |
TCVN 11306:2016 TCVN 6750:2005 US EPA Method 6 US EPA Method 8 US EPA Method 8A |
|
12 |
Nitrous oxide (NOx by NO2) |
TCVN 11307:2016 TCVN 7172:2002 US EPA Method 7 US EPA Method 7E Direct measuring instrument |
TCVN 11307:2016 TCVN 7172:2002 US EPA Method 7 US EPA Method 7A US EPA Method 7B US EPA Method 7C US EPA Method 7D |
|
13 |
Hydrogen sulfide (H2S) |
TCVN 11308:2016 US EPA Method 15 IS K 0108:2010 |
TCVN 11308:2016 IS K 0108:2010 |
|
14 |
Fluorine (F) and F compounds (by fluoride) |
US EPA Method 13A US EPA Method 13B |
US EPA Method 13A US EPA Method 13B TCVN 7243:2003 |
|
15 |
Hydrofluoric acid (HF) |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A TCVN 7244:2003 |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A TCVN 7244:2003 |
|
16 |
Mercury (Hg) and Hg compounds (by Hg) |
TCVN 11311:2016 US EPA Method 29 US EPA Method 30B TCVN 7557-2:2005 |
TCVN 11311:2016 US EPA Method 29 US EPA Method 30B TCVN 7557-2:2005 |
|
17 |
Volatile organic compounds (by TVOC, including constituents of: benzene, toluene, ethylbenzene, xylene, ethyl acetate, butyl acetate) |
CEN/TS 13649:2014 |
CEN/TS 13649:2014 |
|
18 |
Dioxins/Furans (PCDD/PCDF) |
TCVN 11309:2016 TCVN 7556-1:2005 TCVN 5977:2009 US EPA Method 23 US EPA Method 23A EN 1948-1 |
TCVN 11309:2016 TCVN 7556-2:2005 and TCVN 7556-3:2005 US EPA Method 23 EN 1948-2 and Method EN1948-3 |
|
19 |
Hydrogen cyanide (HCN) |
US EPA OTM29 ASTM D7295:06 CEN/TS 17337:2019 ES 01312.a ES 01312.1b ES 01312.2a |
US EPA OTM29 ASTM D7295:06 ES 01312.a ES 01312.1b ES 01312.2a |
|
20 |
Arsenic (As) and As compounds (by As) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
21 |
Chlorine (Cl2) |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A |
|
22 |
H2SO4 vapor |
US EPA Method 8 |
US EPA Method 8 |
|
23 |
Bromine (Br) and Br compounds (by Br2) |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A |
TCVN 11310:2016 US EPA Method 26 US EPA Method 26A |
|
24 |
Carbon disulfide (CS2) |
TCVN 11308:2016 US EPA Method 0031 US EPA Method 15 |
TCVN 11308:2016 |
|
25 |
Acrylonitrile (C3H3N) |
US EPA Method 18 US EPA Method 0030 US EPA Method 0031 ES 01511.1b |
US EPA Method 18 US EPA Method 5040A US EPA Method 5041A ES 01511.1b |
|
26 |
Acetaldehyde (CH3CHO) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
27 |
Aniline (C6H5NH2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
28 |
Benzene (C6H6) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0030 US EPA Method 0031 JIS K 0088:2016 |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5040A US EPA Method 5041A US EPA Method 8260C US EPA Method 8270E JIS K 0088:2016 |
|
29 |
Benzyl chloride (C6H5CH2CI) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
30 |
1,3-Butadiene (C4H6) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0030 ES 01512.1b ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5040A US EPA Method 5041A ES 01512.1b ES 01511.1b |
|
31 |
Butylamine (CH3(CH2)2CH2NH2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
32 |
Cresol (CH3C6H4OH) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
33 |
Chloroform (CHCI3) |
CEN/TS 13649:2014 US EPA Method 0030 US EPA Method 0031 ES 01509.1b ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 5040A US EPA Method 5041A US EPA Method 8270E ES 01509.1b ES 01511.1b |
|
34 |
ß-chloroprene (CH2=CCICH= CH2) |
CEN/TS 13649:2014 US EPA Method 0010 |
CEN/TS 13649:2014 US EPA Method 8260C |
|
35 |
Diethylamine ((C2H5)2NH) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
36 |
Dichloromethane (CH2Cl2) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0030 JIS K 0088:2016 US EPA Method 0031 ES 01513.1b ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5040A US EPA Method 5041A JIS K 0088:2016 ES 01513.1b ES 01511.1b |
|
37 |
1,1-Dichloroethane (CHCI2CH3) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0031 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5041A US EPA Method 8260C ES 01511.1b |
|
38 |
1,2-Dichloroethane (CICH=CHCI) |
CEN/TS 13649:2014 US EPA Method 0010 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 0010 ES 01511.1b |
|
39 |
1,4-Dioxane (C4H8O2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
40 |
Dimethylaniline (C6H5N(CH3)2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
41 |
Dimethyl sulfate ((CH3)2SO4) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
42 |
Ethylamine (CH3CH2NH2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
43 |
Ethylbenzene (CH3CH2C6H5) |
CEN/TS 13649:2014 US EPA Method 0010 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 8260C ES 01511.1b |
|
44 |
Ethyl acrylate (CH2=CHCOO C2H5) |
CEN/TS 13649:2014 US EPA Method 0010 |
CEN/TS 13649:2014 US EPA Method 8260C |
|
45 |
Ethylene oxide (CH2OCH2) |
US EPA Method 431 CEN/TS 13649:2014 ES 01515.1b ES 01515.2b ES 01515.3b |
US EPA Method 431 CEN/TS 13649:2014 ES 01515.1b ES 01515.2b ES 01515.3b |
|
46 |
Formaldehyde (HCHO) |
CEN/TS 17638:2021 US EPA Method 0011 |
CEN/TS 17638:2021 US EPA Method 0011 |
|
47 |
Methanethiol (CH3SH) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 16, 16A, 16B, 16C |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 16, 16A, 16B |
|
48 |
Methyl acrylate (CH2=CHCOO CH3) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
49 |
Methanol (CH3OH) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
50 |
Methyl bromide (CH3Br) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
51 |
Methyl chloride (CH3CI) |
US EPA Method 0030 US EPA Method 18 ES 01511.1b |
US EPA Method 5040A US EPA Method 5041A US EPA Method 8260C ES 01511.1b |
|
52 |
Nitrobenzene (C6H5NO2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
53 |
Phenol and phenol compounds (C6H5OH) |
JIS K 0086:1998 US EPA Method 0010 ES 01503.a ES 01503.1b ES 01503.2a |
JIS K 0086:1998 US EPA Method 8270E ES 01503.a ES 01503.1b ES 01503.2a |
|
54 |
Propylene oxide (C3H6O) |
CEN/TS 13649:2014 ES 01522.1 ES 01522.2 ES 01522.3 |
CEN/TS 13649:2014 ES 01522.1 ES 01522.2 ES 01522.3 |
|
55 |
Styrene (C6H5CH=CH2) |
CEN/TS 13649:2014 US EPA Method 0010 US EPA Method 18 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5041A US EPA Method 8260C ES 01511.1b |
|
56 |
1,1,2,2-Tetrachloroethene (CI2HCCHCI2) |
CEN/TS 13649:2014 US EPA Method 18 |
CEN/TS 13649:2014 US EPA Method 18 |
|
57 |
Tetrachloromethane (CCl4) |
CEN/TS 13649:2014 US EPA Method 0010 US EPA Method 0031 ES 01509.1b ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 5041A US EPA Method 8260C ES 01509.1b ES 01511.1b |
|
58 |
Toluene (C6H5CH3) |
CEN/TS 13649:2014 US EPA Method 0010 US EPA Method 0031 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 8260C US EPA Method 8270E ES 01511.1b |
|
59 |
Trichloroethylene (CICH=CCI2) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0030 US EPA Method 0031 JIS K 0088:2016 ES 01514.1b ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5040A US EPA Method 5041A JIS K 0088:2016 ES 01514.1b ES 01511.1b |
|
60 |
1,1,2-Trichloroethane (CHCI2CH2CI) |
US EPA Method 18 US EPA Method 0030 US EPA Method 0031 ES 01511.1b |
US EPA Method 18 US EPA Method 5040A US EPA Method 5041A US EPA Method 8260C US EPA Method 8270E ES 01511.1b |
|
61 |
Xylene (C6H4(CH3)2) |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0010 ES 01511.1b |
CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5041A ES 01511.1b |
|
62 |
vinyl chloride (CH2=CHCI) |
US EPA Method 106 CEN/TS 13649:2014 US EPA Method 18 US EPA Method 0030 US EPA Method 0031 ES 01509.1b ES 01511.1b |
US EPA Method 106 CEN/TS 13649:2014 US EPA Method 18 US EPA Method 5040A US EPA Method 5041A ES 01509.1b ES 01511.1b |
|
63 |
Particulate matter |
TCVN 5977:2009 US EPA Method 5 US EPA Method 17 ISO 9096:2017 |
TCVN 5977:2009 US EPA Method 5 US EPA Method 17 ISO 9096:2017 |
|
64 |
Lead (Pb) and Pb compounds (by Pb) |
TCVN 11311:2016 US EPA Method 12 US EPA Method 29 TCVN 7557-1:2005 TCVN 7557-3:2005 EN 14385:2004 |
TCVN 11311:2016 US EPA Method 12 US EPA Method 29 TCVN 7557-1:2005 TCVN 7557-3:2005 EN 14385:2004 |
|
65 |
Cadmium (Cd) and Cd compounds (by Cd) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 TCVN 7557-3:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 TCVN 7557-3:2005 |
|
66 |
Chrome (Cr) and Cr compounds (by Cr) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
67 |
Copper (Cu) and Cu compounds (by Cu) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
68 |
Nickel (Ni) and Ni compounds (by Ni) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
69 |
Zinc (Zn) and Zn compounds (by Zn) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
70 |
Antimony (Sb) and Sb compounds (by Sb) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
71 |
Thalium (Tl) and Tl compounds (by Tl) |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 US EPA Method 29 TCVN 7557-1:2005 |
|
72 |
Vanadium (V) and V compounds (by V) |
EN 14385:2004 |
EN 14385:2004 |
|
73 |
Total metal (including: Sb, As, Pb, Cr, Co, Cu, Mn, Ni, V and corresponding compounds) |
TCVN 11311:2016 EN 14385:2004 US EPA Method 29 TCVN 7557-1:2005 |
TCVN 11311:2016 EN 14385:2004 US EPA Method 29 TCVN 7557-1:2005 |
|
74 |
Polycyclic aromatic hydrocarbons - PAH (by equivalent Benzo[a]pyrene) |
TCVN 9237-1:2012 US EPA Method 0023A California EPA Method 429 ES 01505.1a |
TCVN 9237-2:2012 ES 01505.1a |
|
75 |
Smoke opacity |
US EPA Method 9 |
US EPA Method 9 |
|
Note: - TCVN: Vietnam’s National Standards. - CEN/EN: Method dictated by European Committee for Standardization. - US EPA Method: Method of Environmental Protection Agency of the United States. - ASTM: Standard of the American Society for Testing and Materials. - ISO: Standard of International Standard Organization. - JIS: Japanese Industrial Standards. - ES: Standard of South Korea's Ministry of Environment. - IS: Indian Standards. |
|||
Appendix 2
Methods for determining toxicity equivalence (TEQ) of Dioxins/Furans
1. Toxicity Equivalence Factors (TEFs) of 2,3,7,8-Tetrachlorodibenzo-p-dioxin and Dioxin-Like Compounds according to World Health Organization (WHO, 2005):
|
No. |
Dioxins/Furans (PCDD/PCDF) |
|
|
Dioxin-like substance |
TEFs |
|
|
1 |
2,3,7,8 tetrachlorodibenzodioxin (2,3,7,8-TCDD) |
1 |
|
2 |
1,2,3,7,8 pentachlorodibenzodioxin (1,2,3,7,8-PeCDD) |
1 |
|
3 |
1,2,3,4,7,8 hexachlorodibenzodioxin (1,2,3,4,7,8-HxCDD) |
0,1 |
|
4 |
1,2,3,6,7,8 hexachlorodibenzodioxin (1,2,3,6,7,8-HxCDD) |
0,1 |
|
5 |
1,2,3,7,8,9 hexachlorodibenzodioxin (1,2,3,7,8,9-HxCDD) |
0,1 |
|
6 |
1,2,3,4,6,7,8 heptachlorodibenzodioxin (-1,2,3,4,6,7,8-HpCDD) |
0,01 |
|
7 |
octachlorodibenzodioxin (OCDD) |
0,0003 |
|
8 |
2,3,7,8 tetrachlorodibenzofuran (2,3,7,8-TCDF) |
0,1 |
|
9 |
2,3,4,7,8 pentachlorodibenzofuran (2,3,4,7,8-PeCDF) |
0,03 |
|
10 |
1,2,3,7,8 pentachlorodibenzofuran (1,2,3,7,8-PeCDF) |
0,3 |
|
11 |
1,2,3,4,7,8 hexachlorodibenzofuran (1,2,3,4,7,8-HxCDF) |
0,1 |
|
12 |
1,2,3,6,7,8 hexachlorodibenzofuran (1,2,3,6,7,8-HxCDF) |
0,1 |
|
13 |
1,2,3,7,8,9 hexachlorodibenzofuran (1,2,3,7,8,9-HxCDF) |
0,1 |
|
14 |
2,3,4,6,7,8 hexachlorodibenzofuran (2,3,4,6,7,8-HxCDF) |
0,1 |
|
15 |
1,2,3,4,6,7,8 heptachlorodibenzofuran (1,2,3,4,6,7,8-HpCDF) |
0,01 |
|
16 |
1,2,3,4,7,8,9 heptachlorodibenzofuran (1,2,3,4,7,8,9-HpCDF) |
0,01 |
|
17 |
octachlorodibenzofuran (OCDF) |
0,0003 |
2. Formula for calculating TEQ of Dioxins/Furans:
(TEQ)= Σ(Ci x TEFi)
Where:
Ci means concentration of the individual compound.
i means individual compound.
TEFi means toxicity equivalence of corresponding compound.
Appendix 3
Method for calculating Polycyclic aromatic hydrocarbons - PAH (by equivalent Benzo[a]pyrene)
1. Toxicity Equivalence Factors of 16 PAH substances:
|
No. |
Polycyclic aromatic hydrocarbons (PAH) |
|
|
Individual PAH substance |
TEFs |
|
|
1 |
Naphthalene |
0,001 |
|
2 |
Acenaphthene |
0,001 |
|
3 |
Acenapthylene |
0,001 |
|
4 |
Anthracene |
0,0005 |
|
5 |
Benzo[a]anthracene |
0,005 |
|
6 |
Benzo[b]fluoranthene |
0,1 |
|
7 |
Benzo[k]fluoranthene |
0,05 |
|
8 |
Benzo[ghi]perylene |
0,01 |
|
9 |
Benzo[a]pyrene |
1 |
|
10 |
Chrysene |
0,03 |
|
11 |
Dibenz[a,h]anthracene |
1 |
|
12 |
Fluoranthene |
0,05 |
|
13 |
Fluorene |
0,0005 |
|
14 |
Indeno[1,2,3-cd]pyrene |
0,1 |
|
15 |
Phenanthrene |
0,0005 |
|
16 |
Pyrene |
0,001 |
2. Formula for calculating PAH (by Benzo[a]pyrene):
PAH (by Benzo[a]pyrene)= Σ(Ci x TEFi)
Where:
Ci means concentration of individual PAH substance.
i means individual PAH substance.
TEFi means toxicity equivalence of corresponding PAH substance.
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