Environment Quality Act slide in power point ppt

Environment Quality Act slide

1. WELCOME TO
Environmental Quality Act 1974
(EQA 1974)
TRAINING
RAZAK BIN MAJID
Health, Safety and Environment Trainer

2. 2
NAME : Razak Bin Majid
POSITION : Trainer
EDUCATION : Executive Master SHE from UNISEL
H/P : 019-4944324
Competency:
SHO Registered Person (8408)
Train The Trainer (HRDF)
Train The Trainer (BOFA)
Train The Trainer (Forklift)
Train The Trainer (Fire Fighting)
ISO 45001-2018 Lead Auditor
ISO 14001- 2015 Auditor
Authorize Gas Tester (DOSH)
Scaffolder (DOSH)
Traffic Management Supervisor
Lifting Supervisor
Ergonomic Trained Person
Trainer Profile

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Please use nearest exit to the
assembly area
Please do not run
Please do not use the elevator
Use the nearest staircase
Safety Briefing
3

4. Facilities
Washroom (Every floor)

Surau (First Floor)
Cafeteria
Smoking (Ground Floor)
Reminder
Silence hand-phone during training session
Important Things
4

5. Purpose of EQA 1974
INTRODUCTION TO ACT AND REGULATIONS

6. Part I

7. Part I

8. OCCUPIER
OWNER

9. How Many Regulations, Rules and Order Stated In
1.Peraturan Kualiti Alam Sekeliling (Premis Yang Ditetapkan)
(Minyak Sawit Mentah), 1977
2.Peraturan Kualiti Alam Sekeliling (Perlesenan), 1977
3.Peraturan Kualiti Alam Sekeliling (Udara Bersih), 1978
4.Peraturan Kualiti Alam Sekeliling (Penggabungan Kesalahan),
1978
5.Peraturan Kualiti Alam Sekeliling (Premis Yang Ditetapkan)
(Getah Asli Mentah), 1978
6.Peraturan Kualiti Alam Sekeliling (Pengawalan Kepekatan Lead
dalam Bensin Motor), 1985
7.Peraturan Kualiti Alam Sekeliling (Kebisingan Kenderaan
Bermotor), 1987
8.Perintah Kualiti Alam Sekeliling (Aktiviti Yang Ditetapkan)
(Penilaian Kesan Alam Sekitar), 1987
9.Peraturan Kualiti Alam Sekeliling (Premis yang Ditetapkan)
(Jadual Kemudahan Rawatan dan Pembuangan Sampah), 1989

10. 11.Peraturan Kualiti Alam Sekeliling (Jadual Pembaziran), 1989
12.Perintah Kualiti Alam Sekeliling (Delegasi Kuasa Mengawal
Pencemaran Laut), 1993
13.Perintah Kualiti Alam Sekeliling (Larangan penggunaan Bahan
Terkawal dalam Sabun, Pencuci Sintetik dan Ejen Pembersih Lain),
1995
14.Peraturan Kualiti Alam Sekeliling (Kawalan Pelepasan dari Mesin
Diesel), 1996
15.Peraturan Kualiti Alam Sekeliling (Kawalan Pelepasan dari Mesin
Petrol), 1996
16.Peraturan Kualiti Alam Sekeliling (Pengurusan Halon), 1999
17.Peraturan Kualiti Alam Sekeliling (Pengurusan Penyejuk), 1999
18.Peraturan Kualiti Alam Sekeliling (Penggabungan Kesalahan)
(Pembakaran Terbuka), 2000
19.Perintah Kualiti Alam Sekeliling (Delegasi Kuasa) (Penyiasatan
Pembakaran Terbuka), 2000
How Many Regulations, Rules and Order Stated In

11. 20.Perintah Kualiti Alam Sekeliling (Delegasi Kuasa) (Pengurusan
Halon), 2000
21.Perintah Kualiti Alam Sekeliling (Delegasi Kuasa) (Perbadanan
Putrajaya), 2002
22.Peraturan Kualiti Alam Sekeliling (Lembaga Rayuan), 2003
23.Peraturan Kualiti Alam Sekeliling (Kawalan Pelepasan dari
Motosikal), 2003
24.Perintah Kualiti Alam Sekeliling (Aktiviti yang Diisytiharkan)
(Pembakaran Terbuka), 2003
25.Peraturan Kualiti Alam Sekeliling (Dioksin dan Furan), 2004
26.Peraturan Kualiti Alam Sekeliling (Jadual Pembuangan), 2005
How Many Regulations, Rules and Order Stated In

12. 27.Perintah Kualiti Alam Sekeliling (Penyampaian yang Ditetapkan)
(Pembaziran Jadual), 2005
28.Perintah Kualiti Alam Sekeliling (Delegasi Kuasa), 2005
29.Peraturan-Peraturan Kualiti Alam Sekeliling (Pengendalian Properti
Petrol dan Diesel), 2007
30.Peraturan Kualiti Alam Sekeliling (Pembaziran Jadual) (Pindaan), 2007
31.Peraturan Kualiti Alam Sekeliling (Kumbahan), 2009
32.Peraturan Kualiti Alam Sekeliling (Pengawalan Pencemaran Dari
Stesen Pemindahan Sisa Pepejal dan TPA), 2009
33.Peraturan Kualiti Alam Sekeliling (Efluen Industri), 2009
How Many Regulations, Rules and Order Stated In

13. •Part I – Preliminary
•Part II – Administration
•Part III – Licenses
•Part IV – Prohibition and Control of Pollution
•Part IVA – Control of Schedule Wastes
•Part V – Appeal and Appeal Board
•Part VA – Payment of Cess and Environmental Fund
•Part VI – Miscellaneous
INTRODUCTION TO ENVIRONMENTAL
QUALITY ACT, 1974
Arrangement of regulation

14. Bahagian I (Permulaan)
Seksyen 1 - Tajuk ringkas, pemakaian dan mula berkuatkuasa.
Seksyen 2 - Tafsiran.
Bahagian II (Pentadbiran)
Seksyen 3 – 9
Bahagian III (Lesen)
Seksyen 10 – 17
Bahagian IV (Larangan Dan Kawalan Mengenai Pencemaran)
Seksyen 18 – 34A
Bahagian IVA (Kawalan Buangan Terjadual)  
Seksyen 34B
Bahagian V (Rayuan Dan Lembaga Rayuan)
Seksyen 35 – 36
Bahagian VI (Pembayaran Ses Dan Kumpulan Wang Alam Sekeliling)
Seksyen 37 - 51

20. ENVIRONMENTAL QUALITY
(CLEAN AIR) REGULATIONS, 2014
Arrangement of regulation
1.Obligation to comply and notify
2.Measures to reduce emission
3.Air pollution control systems, performance, failure
4.Maintenance of record
5.Limit value and technical standard
6.Monitoring
7.Emission declaration

21. CAR 2014 vs CAR 1978
30 Regulations
6 Schedules
2014
21
Number of Regulations & Schedules
1978
59 Regulations
5 Schedules
All premises
General standard
emission
SECOND
SCHEDULE
Specific standard for
specific industry
11 specific industries
(Table A – K)
THIRD
SCHEDULE
Toxicity equivalents
factor (TEFs) for dioxin
and furan
FOURTH
SCHEDULE
Emission Standards For
Hazardous Substances
6 Categories (Category
1 – 6)
FIFTH
SCHEDULE
List of Undesirable
Occurrence
SIXTH
SCHEDULE
ACTIVITY
COMPLIANCE
SUBJECT TO
SCHEDULE

22. Regulation 12(1)
Not darker than
shade No 1
Ringelmann Chart
Not greater than
20% opacity
Transmissometer
(1 minute averaging
time )
Regulation 12(2)
12(2)(a) No 2
Ringelmann Chart in
5 minutes aggregate
within 1 hour period
12(2)(a) No 2
Ringelmann Chart in
15 minutes aggregate
within 24 hours period
12(2)(b) At Start-up
No 2 Ringelmann
Chart
Regulation 12(3)
Premise emitting
≥ 2.5 kg/hour dust
or potentially
emitting smoke
darker than No 2
Ringelmann Chart
shall operate a
transmissometer
(averaging time: 1
minute)
REGULATION

23. 23
OBLIGATION TO COMPLY
EXISTING PREMISES
COMPLIANCE
NEW PREMISES
Premises purchased or
acquired on or after the
date CAR 2014 come
into operation
COMPLIANCE
EXISTING PREMISES
Existing premises or
premises in operation
before CAR 2014 come
into operation
COMPLIANCE
PREMISES WITH
COMPLAINTS
Director General may serve
upon the owner or occupier a
notice in writing requiring
complying to the CAR 2014.
The 5 years grace period is
not applicable for these cases

24. OBLIGATION TO NOTIFY

25. Generator
Spray
Booth
Scrubber
Bag
Filter
ESP
Centrifugal
Dust
Collector
Incinerator
Fuel Burning
Equipment
AS/PUB/N-APB
AS/PUB/N-SCRUBBER
AS/PUB/N-BAGFILTER
AS/PUB/N-INS
AS/PUB/N-JANA
AS/PUB/N-CYCLONE
AS/PUB/N-ESP
AS/PUB/N-SPRAYBOOTH
NOTIFICATIO
N FORMS
OBLIGATION TO NOTIFY

26. BAT
Best
techniques
and effective
way to
prevent and
reduce
pollution
Size, design and operating characteristics of the plant or the
latest process
Selection of raw material or fuel
Implementation of the 3R concept
Other processes within the plant design capacity & capability
Other way of operating or setting within the plant design capacity
& capability
Proper handling & monitoring
Efficient and continuous maintenance of a plant & equipment
Reasonable economic & cost factors
INDUSTRY LISTED IN THE 1
ST
SCHEDULE (CAR 2014)
BAT DOCUMENTS
MEASURES TO REDUCE EMISSION

27. PRE-REQUISITE FOR SUCCESSFUL AIR POLLUTION
CONTROL SYSTEMS
Quality Construction
and Installations
Proper Operation
and Maintenance
Adequately Design of
APC

28. AIR POLLUTION CONTROL SYSTEM
30days afterpremises
operation :
1.Written declaration
2.As-built drawing
start
28
Sound Engineering Practices
To ensure that all components of APCS are in good condition working
Specification as in Guidance Document for Fuel Burning Equipment And Air
Pollution Control Systems (GD APCS)

29. AIR POLLUTION
What is air pollution?

32. CONTROL OF AIR POLLUTION
To control particulate emissions following equipments are
employed:-
Settling chambers
Cyclone separators
Fabric filters
Electrostatic precipitators
Wet collector

35. Telephone SMS E-mail Fax
35
MODE OF
NOTIFICATION
Failure In Operations Of Air Pollutions
Control System
The DG should be notified not later than 1 hour.

36. LIMIT VALUE AND TECHNICAL
STANDARD
STANDARD
KONSEP STANDARD DALAM
PERATURAN UDARA BERSIH

37. All industries under 1
ST
Schedule must comply to standards in 2
nd
& 3
rd
Schedule
LIMIT VALUES AND TECHNICAL
STANDARDS
Fuel Burning Equipment (FBE)
using:-
pulverized fuel
any solid fuel ≥ 30 kg/hr.
any liquid or gaseous matter≥15
kg/hr. have to comply with the
standards specified in 2
nd Schedule.
1.Heat and Power Generation
2.Production and Processing of Ferrous Metals
(Iron and Steel Mills)
3.Ferrous Metal Foundries
4.Production and Processing of
5.Non-Ferrous Metals
6.Oil and Gas industry
7.Non-Metallic (Mineral) Industry :
All sizes cement
8.Asphalt Mixing Plant (Stationary
Installations)
9.Pulp and Paper Industry
10.Chemical and Petrochemical
Industry
11.Solvent Use in Industry
12.Waste Incinerators

38. Fuel typeFuel Fuel quality parameter
Liquid AllSulphur content < 500 ppm (per weight)
Solid
CoalSulphur content < 1% (per weight)
Biomass
Wood, agricultural waste, etc.: air dry and in its
natural composition (e.g. wood without coating, paint
or other treatment)
Residues from wood-based industries: without wood
preservatives
Second (2
nd
) Schedule
(I) Control of fuel burning equipment, incinerators and crematoria
1.Control of fuel quality for fuel burning equipment and incinerators not covered
by the
LIMIT VALUES AND TECHNICAL
STANDARDS
FIRST SCHEDULE

39. Second (2
nd
) Schedule
2. Combustion emissions from fuel burning equipment and incinerators not
covered
Fuel type Pollutant Limit valueMonitoring
Liquid
Total particulate matter (PM)
Where dust load emitted :
a) > 0.33 < 1.0 kg/h
b) ≥ 1.0 kg/h
50 mg/m
3
Once/year
2 times/year
Solid
Total particulate matter (PM)
Where dust load emitted : a)> 0.44 <
1.0 kg/h
b)≥ 1.0 < 1.5 kg/h
c)≥ 1.5 < 2.0 kg/h
d)≥ 2.0 < 2.5 kg/h
e)≥ 2.5 kg/h
150 mg/m³
Once/year 2
times/year
3times/year
4times/year
Continuous*
Carbon monoxide (CO) 1000 mg/m³Periodic
CO
2 reference content is 12%
* Averaging time for continuous monitoring is 30 minutes
LIMIT VALUES AND TECHNICAL
STANDARDS
BY THE FIRST SCHEDULE

40. •Control of NMVOC
Emission Outlets
Halogenated hydrocarbons
– 20 mg/m
3
Others – 150 mg/m
3
•Control of Fugitive
Emissions
•Refer Guidance Document
of Fugitive Emission
Control
Third (3
rd
) Schedule
i.2
nd
Schedule limits applies to all
industries if not specified in 3
rd
Schedule;
ii.Specific industry in the title;
iii.Capacities are stipulated in the
title;
iv.Percentage of O
2 or CO
2 reference
content differ base on process and
industry;
v.Limit values are normalized;
vi.Monitoring type: Periodic or
Continuous; and
vii.“Note” at the bottom of each
sub-table is important
LIMIT VALUES AND TECHNICAL
STANDARDS
Second (2
nd
) Schedule

41. 1. Boiler O
2 reference content is 6% for solid fuels and 3% for others.
HEAT AND POWER GENERATION
MW
e = electrical
power
3
rd SCHEDULE
* Averaging time for continuous monitoring is 30 minutes
Fuel type Pollutant Capacity Limit value Monitoring
Solid and
liquid fuels
Sum of SO
2 and SO
3, expressed as SO
2 > 10 MW
e 500 mg/m³ Continuous*
Sum of NO and NO
2 expressed as NO
2 > 10 MW
e 500 mg/m³ Continuous*
Hydrogen chloride (HCl) > 10 - <100
MW
e
200 mg/m³ Periodic
Hydrogen chloride (HCl) ≥100 MW
e 100 mg/m³ Periodic
Hydrogen fluoride (HF) > 10 - <100
MW
e
30 mg/m³ Periodic
Hydrogen fluoride (HF) ≥100 MW
e 15 mg/m³ Periodic
Carbon monoxide (CO) > 10 MW
e 200 mg/m³ Continuous*
Total PM > 10 MW
e 50 mg/m³ Continuous*
Mercury (Hg) >10 MW
e 0.03 mg/m³ Periodic
PCDD/PCDF > 10 MW
e 0.1 ng TEQ/m
3
Periodic
Gaseous fuelsSum of NO and NO
2 expressed as NO
2 > 10 MW
e 350 mg/m³ Continuous*
Carbon monoxide (CO) > 10 MW
e 50 mg/m³ Continuous*
Total PM 29 > 10 MW
e 5 mg/m³ Periodic

42. Fuel type Pollutant
Capacity at ISO
conditions Limit value Monitoring
Gaseous fuels
Sum of NO and NO
2 expressed
as NO
2
> 10 MW
e 150mg/m³ Continuous*
Carbon monoxide (CO) > 10 MW
e 100 mg/m³ Continuous*
Liquid fuels
Sum of NO and NO
2 expressed
as NO
2
> 10 MW
e 200 mg/m³ Continuous*
Carbon monoxide (CO) > 10 MW
e 100 mg/m³ Continuous*
2. Combustion turbines
O
2 reference content is 15%.
* Averaging time for continuous monitoring is 30
minutes
3. Generator sets for combined heat and power production with a total thermal output ≥ 3
MW
e:
Fuel type Pollutant Capacity Limit value Monitoring
Liquid or gas fuels
Sum of NO and NO
2
expressed as NO
2
≥ 3 MW
e 600mg/m³ Periodic
Carbon monoxide (CO) ≥ 3 MW
e 650 mg/m³ Periodic
Total PM ≥ 3 MW
e 80 mg/m
3
Periodic
O
2 reference content is 5%.

43. PRODUCTION AND PROCESSING OF
FERROUS METALS (IRON AND STEEL MILLS)
Source Pollutant Limit valueMonitoring
Sinter plants (waste gas from the
sintering belt)
Sum of SO
2 and SO
3, expressed as
SO
2
500mg/m³ Continuous*
Sum of NO and NO
2 expressed as
NO
2
400 mg/m³ Continuous*
Total PM 50 mg/m³ Continuous*
Total lead as Pb 1 mg/m
3
Periodic
NMVOC 75 mg/m
3
Periodic
PCDD/PCDF 0.1 ng TEQ/m
3
Periodic
Coke ovens (@ 5% O
2)
Total PM 10 mg/m
3
Continuous*
Sum of NO and NO
2 expressed as
NO
2
500 mg/m³ Periodic
Sulphur compounds as S 800 mg/m³ Periodic
Blast furnace (Regenerator; @ 3%
O
2)
Total PM 50 mg/m
3
Continuous*
Basic oxygen furnace (converter
gas)
Total PM 50 mg/m
3
Continuous*
Electric arc furnaces Total PM 50 mg/m
3
Continuous*
Rolling mill: Thermal treatment
furnace
(@ 5% O
2)
Sum of NO and NO
2 expressed as
NO
2
500 mg/m³ Periodic
* Averaging time for continuous monitoring is 30 minutes

44. Source Pollutant Limit valueMonitoring
Cupola furnace
Sum of SO
2 and SO
3,
expressed as SO
2
500mg/m³ Periodic
Carbon monoxide (CO)150 mg/m³ Periodic
Core production and
casting
Amine 5 mg/m
3
Periodic
Benzene 5 mg/m
3
Periodic
FERROUS METAL FOUNDRIES
WITH A CAPACITY ≥ 1 TON
MOLTEN METAL PER DAY

45. PRODUCTION AND PROCESSING OF NON-
FERROUS METALS WITH A CAPACITY ≥ 0.5 TONS
PER DAY FOR LEAD OR CADMIUM OR ≥ 2 TONS
PER DAY FOR OTHER METALS
* Averaging time for continuous monitoring is 30 minutes
Source Pollutant Limit value Monitoring
Sinter plants (waste gas
from the sintering belt)
Sum of SO
2 and SO
3, expressed as SO
2500mg/m³ Continuous*
Sum of NO and NO
2 expressed as NO
2400 mg/m³ Continuous*
Total PM 50 mg/m³ Continuous*
Total lead as Pb 1 mg/m
3
Periodic
NMVOC 75 mg/m
3
Periodic
PCDD/PCDF 0.1 ng TEQ/m
3
Periodic
Production of copper and
zinc
Total PM 20 mg/m
3
Continuous*
Production of lead Total PM 10 mg/m
3
Continuous*
Primary aluminium
Total PM 10 mg/m
3
Continuous*
Fluorine compounds as HF 1 mg/m
3
Periodic
Total Fluoride 1.5 mg/m
3
Periodic
Sum of SO
2 and SO
3, expressed as SO
2
100 mg/m
3
Continuous*

46. Source Pollutant Limit value Monitoring
Secondary aluminium
1)
Total PM 10 mg/m
3
Continuous*
Sum of NO and NO
2
expressed as NO
2
500 mg/m³ Periodic
Smelting, alloying and
refining
of aluminium
2)
Total PM 10 mg/m
3
Continuous*
Smelting, alloying and
refining of other non-
ferrous metals
Total PM 5 mg/m
3
Continuous*
* Averaging time for continuous monitoring is 30 minutes
1.In secondary aluminium production, hexachloroethane shall not
be used for smelting. “Secondary aluminium” is defined as re-
melting of all kinds of used aluminium end products which
might be coated, painted, and laminated.
2.“Smelting, alloying and refining of aluminium” is defined as
melting of pure aluminium and plain scrap.

47. Source Pollutant Limit value Monitoring
Claus plant Sulphur Recovery > 95% Periodic
Catalytic cracking
Total PM 40 mg/m
3
Continuous*
Sum of SO
2 and SO
3,
expressed as SO
2
1200 mg/m
3
Continuous*
Calcination Total PM 40 mg/m
3
Continuous*
OIL AND GAS INDUSTRIES: REFINERIES
(ALL SIZES); NATURAL GAS PROCESSING
AND STORAGE; STORAGE AND
HANDLING OF PETROLEUM PRODUCTS
* Averaging time for continuous monitoring is 30
minutes

48. Source Pollutant Limit value Monitoring
Cement kilns
Sum of NO and NO
2 expressed as NO
2 800 mg/m
3
Continuous*
Total PM 50 mg/m
3
Continuous*
Mercury 0.05 mg/m
3
Periodic
PCDD/PCDF 0.1 ng TEQ/m
3
Periodic
Rotary furnaces for the
manufacture of hard
quicklime or sintering
dolomite
Sum of NO and NO
2 expressed as NO
2 1500 mg/m
3
Continuous*
Total PM 50 mg/m
3
Continuous*
Mercury 0.05 mg/m
3
Periodic
PCDD/PCDF 0.1 ng TEQ/m
3
Periodic
O
2 reference content for:
a)cement kilns is 10%
b)flame-heated glass melting furnaces is 8%
c)flame-heated pot furnaces and day tanks furnaces 13 %
d)ceramic furnaces is 17%
NON-METALLIC (MINERAL) INDUSTRY: CEMENT
PRODUCTION (ALL SIZES); MANUFACTURE OF GLASS
INCLUDING GLASS FIBRE WITH A MELTING CAPACITY ≥
1 TON OF PRODUCT PER DAY; MANUFACTURE OF
CERAMIC PRODUCTS BY FIRING, ROOFING TILES,
BRICKS, REFRACTORY BRICKS, TILES, CERAMIC GLASS,
STONEWARE OR PORCELAIN, WITH A PRODUCTION
CAPACITY ≥ 10
TONS OF PRODUCT PER DAY
* Averaging time for continuous monitoring is 30
minutes

49. Source Pollutant Limit value Monitoring
Glass furnaces
Sum of SO
2 and SO
3, expressed as
SO
2
800 mg/m
3
Continuous*
Sum of NO and NO
2 expressed as
NO
2
800 mg/m
3
Continuous*
Total lead as Pb 5 mg/m
3
Periodic
Total PM 50 mg/m
3
Continuous*
Ceramic furnaces
Sum of SO
2 and SO
3, expressed as
SO
2
800 mg/m
3
Periodic
Sum of NO and NO
2 expressed as
NO
2
800 mg/m
3
Periodic
Total PM
Where dust load emitted :
a)> 0.33 < 1.0 kg/h
b)≥ 1.0 <2.0 kg/h
c)≥ 2.0 kg/h
50 mg/m
3 Once/year 2
times/year
Continuous*
* Averaging time for continuous monitoring is 30
minutes

50. Fuel type Pollutant Limit value Monitoring
Liquid and gaseousCarbon monoxide (CO) 0.50 g/m³ Periodic
Solid Carbon monoxide (CO) 1.0 g/m³ Periodic
All fuels
Total PM 50mg/m³ Periodic
NMVOC 50 mg/m³ Periodic
O
2 reference content is17%.
ASPHALT MIXING PLANTS
(STATIONARY INSTALLATIONS)

51. Source Pollutant Limit value Monitoring
Recovery furnaces
PM 150 mg/m
3
Periodic
Sum of NO and NO
2
expressed as NO
2
2 kg/t Air Dried Pulp
(ADP)
Periodic
Lime kilns
Hydrogen sulfide (H
2S) 15 mg/m
3
Periodic
Sum of NO and NO
2
expressed as NO
2
2 kg/t Air Dried Pulp
(ADP)
Periodic
Sulfite mills Total sulfur
1.5 kg/t Air Dried
Pulp (ADP)
Periodic
Kraft and othersTotal sulfur
1.0 kg/t Air Dried
Pulp (ADP)
Periodic
PULP AND PAPER INDUSTRY INCLUDING
PAPER RECYCLING FACILITIES IN ALL
SIZES

52. Pollutant Limit value Monitoring
Hydrogen chloride (HCl)200 mg/m
3
Periodic
Sum of NO and NO
2
expressed as
NO
2
700 mg/m
3
Periodic
Ammonia (NH
3) 76 mg/m
3
Periodic
Chlorine (Cl) 32 mg/m
3
Periodic
Sum of SO
2 and SO
3,
expressed as SO
2
100 mg/m
3
Periodic
Mercury (Hg) 0.05 mg/m
3
Periodic
Hydrogen Sulphide (H
2S) 7.5 mg/m
3
Periodic
Total PM 50 mg/m
3
Periodic
CHEMICAL AND PETROCHEMICAL
INDUSTRY IN ALL SIZES

53. 1.Facilities of this category shall establish a solvent management plan in order to set-up
a reduction strategy.
2.Solvent losses shall be reduced in accordance with Best Available Techniques
Economically Achievable limiting these losses to not more than 30% of the solvent
input as a general rule.
3.Actual reduction targets and their time frame shall be set on a case-by-case basis as
outlined in the Guidance Document on Fugitive Emission Control.
SOLVENT USE IN INDUSTRY: FACILITIES FOR THE SURFACE
TREATMENT OF SUBSTANCES, OBJECTS OR PRODUCTS USING
ORGANIC SOLVENTS, IN PARTICULAR FOR DRESSING,
PRINTING, COATING, DEGREASING, WATERPROOFING, SIZING,
PAINTING, CLEANING OR IMPREGNATING, FAT EXTRACTION,
WITH A SOLVENT CONSUMPTION CAPACITY OF MORE THAN
200 TONNES PER YEAR

54. Pollutant Limit value Monitoring
Total PM 100 mg/m
3
Continuous*
NMVOC as total organic carbon 10 mg/m
3
Continuous*
Hydrogen chloride (HCl) 40 mg/m
3
Continuous*
Hydrogen fluoride (HF) 1 mg/m
3
Continuous*
Sum of SO
2 and SO
3, expressed as SO
2 50 mg/m
3
Continuous*
Sum of NO and NO
2 expressed as NO
2 200 mg/m
3
Continuous*
Carbon monoxide (CO) 50 mg/m
3
Continuous*
Cadmium and its compounds, expressed as cadmium (Cd)
Thallium and its compounds, expressed as thallium (Tl)
Total
0.05 mg/m
3
Periodic
Mercury and its compounds, expressed as mercury (Hg) 0.05 mg/m
3
Periodic
Antimony (Sb), Arsenic (As), Lead (Pb), Chromium (Cr), Cobalt
(Co), Copper
(Cu), Manganese (Mn), Nickel (Ni), Vanadium (V), and their
compounds expressed as the element
Total
0.5 mg/m
3
Periodic
PCDD/PCDF 0.1 ng TEQ/m
3
Periodic
O
2
reference content is 11%.
WASTE INCINERATORS IN ALL
SIZES
* Averaging time for continuous monitoring is 30 minutes

55. Chlorine Position Component Equivalents Factor
DIOXIN
(a)2,3,7,8 Tetraklorodibenzodioksin (TCDD) 1
(b)1,2,3,7,8 Pentaklorodibenzodioksin (PeCDD) 0.5
(c)1,2,3,4,7,8 Heksaklorodibenzodioksin (HxCDD) 0.1
(d)1,2,3,7,8,9 Heksaklorodibenzodioksin (HxCDD) 0.1
(e)1,2,3,6,7,8 Heksaklorodibenzodioksin (HxCDD) 0.1
(f)1,2,3,4,6,7,8 Heptaklorodibenzodioksin (HpCDD) 0.01
(g)1,2,3,4,6,7,8,9 Oktaklorodibenzodioksin (OCDD) 0.001
FURAN
(a)2,3,7,8 Tetraklorodibenzofuran (TCDF) 0.1
(b)2,3,4,7,8 Pentaklorodibenzofuran (PeCDF) 0.5
(c)1,2,3,7,8 Pentaklorodibenzofuran (PeCDF) 0.05
(d)1,2,3,4,7,8 Heksaklorodibenzofuran (HxCDF) 0.1
(e)1,2,3,7,8,9 Heksaklorodibenzofuran (HxCDF) 0.1
(f)1,2,3,6,7,8 Heksaklorodibenzofuran (HxCDF) 0.1
(g)2,3,4,6,7,8 Heksaklorodibenzofuran (HxCDF) 0.1
(h)1,2,3,4,6,7,8 Heptaklorodibenzofuran (HpCDF) 0.01
(i)1,2,3,4,7,8,9 Heptaklorodibenzofuran (HpCDF) 0.01
(j)1,2,3,4,6,7,8,9 Oktaklorodibenzofuran (OCDF) 0.001
44
TOXICITY EQUIVALENTS FACTOR (TEFs) FOR DIOXIN AND
FURAN
Forth (4
th
) SCHEDULE

56. Bacaan
normalized
pada STP
(273K,
101.3
kPa)
Tentukan
rujukan O
2
yang
ditetapkan
Contoh :
Bagi loji janakuasa menggunakan bahanapi
pepejal, rujukan oksigen adalah 6% dan nilai
had pengeluaran NO
2 adalah 500 mg/m
3. Jika
bacaan yang diukur adalah 490 mg/m
3 pada
bacaan oksigen 8%, maka bacaan yang diukur
perlu normalized dengan menggunakan formula
berikut:
O2, ref
[G
N] 20.9
O2,
measured
= O
2 reading, % vol
= reference oxygen content, % vol
[G] = measured gas concentration
= normalized gas concentration
= percentage of oxygen in ambient
air

2,measured
2,ref20.9  O

G
N
G
20.9 
O
3
m
G
N
 566
mg
20.9  8490
20.9  6

57. Bacaan
normalized
pada STP
(273K,
101.3
kPa)
Tentukan
rujukan
CO
2
adalah
12%
Contoh :
Bagi pelepasan daripada peralatan pembakaran bahanapi yang menggunakan bahanapi
pepejal, rujukan karbon dioksida adalah 12% dan nilai had pengeluaran jirim zarahan
(PM) adalah 150 mg/m
3. Jika bacaan yang diukur adalah 140 mg/m
3 pada bacaan karbon
dioksida 8%, maka:
CO
2, ref
N
CO
CO
2,ref
2,measured
G
G
12
 210
mg
m
3
G
N  140
8
PELEPASAN KARBON
MONOKSIDA
CO
2, measured = CO
2 measured, % vol
= reference carbon dioxide content, %
vol
[G] = measured gas
concentr
D
at
it
io
e
n
tapkan mengikut
keperluan
[G
N] = normalized gas
concent(rcaatiosen to case basis) bagi
proses
yang memerlukan pembakaran
tidak lengkap seperti kilang
penghasilan kayu arang (kiln)

58. MONITORING
MONITORING
carry out as
specified in
relevant schedules
carry out between 3
months to 6 months from
commencement of
operation
record kept
for
3 years
analyzed by
accredited lab
once a year by
competent
person
carried out in a
representative condition
(normal/optimum
condition)
58

59. 59
•in the case of an existing premises, no later than
eighteen months from the date on which these
Regulations come into operation; and
•in the case of a new premises, the first emission
declaration shall be submitted twelve months after the
date the facility commences its operations, but no later
than eighteen months from such date
The emission declaration shall be submitted as follows:
A.
B.
An owner or occupier of a premises which carries out any of the activities or
industries specified in the First Schedule shall for every calendar year submit to
the Director General an emission declaration in such form as determined by the
Director General.
EMISSION DECLARATION

60. ENVIRONMENTAL QUALITY (INDUSTRIAL
EFFLUENT) REGULATIONS, 2009
Arrangement of regulation
1.Obligation to notify Director General
2.Design and construction of industrial effluent treatment system
3.Compliance with specification of industrial effluent treatment system
4.Monitoring of discharge
5.Competent person
6.Acceptable condition for the discharge of industrial of (COD)
7.Prohibition discharge through by pass
8.Spill, accidental discharge or leaking
9.Maintenance record

61. INDUSTRIAL EFFLUENT
TREATMENT SYSTEMS
Industrial Effluent Treatment
Systems :
Performance monitoring :

63. WWTP
WWTP can consist one
or several process to treat
the influent :
•Preliminary
(Pre – Treatment)
•Primary Treatment
•Secondary Treatment
•Tertiary Treatment
01 02 03

64. OBLIGATION TO NOTIFY DIRECTOR
GENERAL
a.
b.
c.
d.

65. OBLIGATION TO NOTIFY DIRECTOR
GENERAL
(2)

66. DESIGN AND COSTRUCTION OF
INDUSTRIAL EFFLUENT TREATMENT
SYSTEMS

67. DESIGN AND COSTRUCTION OF
INDUSTRIAL EFFLUENT TREATMENT
SYSTEMS

68. COMPLIANCE WITH SPECIFICATIONS
OF INDUSTRIAL EFFLUENT
TREATMENT SYSTEM

69. MONITORING OF DISCHARGE

70. MONITORING OF DISCHARGE

71. COMPETENT PERSON

72. ACCEPTABLE CONDITION FOR THE
DISCHARGE OF INDUSTRIAL OF (COD)

73. ACCEPTABLE CONDITION FOR THE
DISCHARGE OF INDUSTRIAL OF
(COD)

74. ACCEPTABLE CONDITION FOR THE
DISCHARGE OF INDUSTRIAL
OF(COD)

75. PROHIBITION DISCHARGE
THROUGH BY PASS

76. SPILL ACCIDENTAL DISCHARGE OR
LEAKING

77. SPILL ACCIDENTAL DISCHARGE OR
LEAKING

78. SPILL ACCIDENTAL DISCHARGE OR
LEAKING

79. MAINTENANCE OF RECORD

80. Physico – Chemical ProcessesBiological Processes
EXAMPLE OF PERFORMANCE MONITORINGEXAMPLE OF PERFORMANCE MONITORING

81. Waste Water Treatment Plant
SAMPLING METHODSAMPLING METHOD
IN-SITU COMPOSITEGRAB

83. Waste Water Treatment Plant
CLARIFICATION OF STANDARD
A AND B
Regulations 12 and Standard of Final Discharge clarification

84. COMMON IETS USED IN INDUSTRIES IN MALAYSIACOMMON IETS USED IN INDUSTRIES IN MALAYSIA
PHYSCIO – CHEMICAL
TREATMENT PROCESSES
Chemical Precipitation
Oxidation / Reduction
Dissolved Air Floatation (DAF)
BIOLOGICAL TREATMENT
PROCESSES
Activated Sludge
Sequential Batch Reactor
Oxidation Ponds
Trickling Filter
Anaerobic Up flow Sludge Blanket
(AUSB)
ADVANCED TREATMENT
PROCESSES
Ion Exchange
Activated Carbon Adsorption
Filtration
TREATMENT OF SLUDGE
Sludge drying bed
Filter Press
Screw Press
Belt Press
Centrifugal separation

85. CLASSIFICATION OF TREATMENT PROCESSCLASSIFICATION OF TREATMENT PROCESS

86. WWTP TRENCH (BAR SCREEN)WWTP TRENCH (BAR SCREEN)
•Function to block any carry over lump from the Pre-Treatment.
•Prevent any trash from entering the Equalizer Tank / System.
WWTP TRENCH A WWTP TRENCH B

88. ENVIRONMENTAL QUALITY
(SEWAGE) REGULATIONS, 2009

90. SEWAGE

91. TYPE OF WASTE

92. TYPE OF WASTE

93. SEWAGE TREATMENT

94. Sewage treatment generally involves three stages-
PRIMARY TREATMENT
SECONDARY TREATMENT
TERTIARY TREATMENT

95. PRIMARY
TREATMENT

96. BAR SCREENING

97. SECONDARY TREATMENT
Secondary sedimentation tank

98. Methods of tertiary treatment-
Filtration
Sludge drying beds
Chlorination
TERTIARY TREATMENT

99. Why Implement Waste Acceptance Criteria?

100. DOE Baseline
WAC
Validate with DOE Baseline
for Comply Treatment &
Composition
Disposal Only
Recovery
Recycle
1
First validation
on the Waste
allowed Recycle
2
Mapping
Composition
to Possible
Treatment
3
Final options if no
possible handling
types fits in
Required
Periodic
Compliance
Required to
Report
Residue

101. DOE Baseline
WAC
1
Validate the Range
of Treatment &
Composition value
with Baseline
Waste Receiver
Validate with DOE
Baseline for Comply
Treatment & Composition
3
Waste Generator
2
Waste Receiver,
Composition Map
Compiled Library
4
Get Matching
Treatment, and
Search for Receiver
Eligible
Receiver
Select Handling &
Submit CN
Transfer to
Receiver

102. Internal System Flows for Waste Generator
& Receiver
•Waste
Characteristic
•Component List
**Upload Lab Report
Qualified
WR
•List of Matching
WR according
to Composition
Values
•**Preferred WR
WAC Range
& Limits

103. 103 103
Waste
Generator
Waste
Receiver
L
i
c
e
n
s
e

&

W
a
s
t
e

C
o
d
e
Notification
Waste
Handling
(TWG)
Consignment
Note
Product
Residue
MASS
BALANCE
•Lampiran E
Inventory
•Handling
•Residue
(Recover,
Recycle)
•Receiving
eSWIS WAC Framework Overview
TWG
Submission
•Lampiran A
Acknowledgement
Special
Management
Composition
Map
Component Baseline
DOE WAC
Governance
Waste
Acceptance
Criteria
Waste
Characteristic
WAC
Matching
Generator
WAC
Allowed
Receiver
DOE

104. SCHEDULE WASTE
MANAGEMENT APPROACH

105. SOURCE OF SCHEDULE WASTE

106. Hazardous waste
characteristics
Hazardous waste defined by the
following the characteristics which
are:
Ignitability
Corrosivity
Toxicity
Reactivity
Infectious or pathogenic

109. MALAYSIAN SCHEDULED WASTE
MANAGEMENT AND POLICY

111. ENVIRONMENTAL QUALITY (SCHEDULED
WASTE) REGULATIONS, 2005
Arrangement of regulation
1.Competence person and function
2.Spill or accidental discharge from sewage
3.Maintenance record

112. SPILL OR ACCIDENTAL
DISCHARGE OF SEWAGE

113. SPILL OR ACCIDENTAL
DISCHARGE OF SEWAGE

114. SPILL OR ACCIDENTAL
DISCHARGE OF SEWAGE
5)Where the Director General undertakes to cleanse or abate any
spill or accidental discharge, he shall determine the full costs
and expense incurred and may recover such costs and expenses
from the owner or occupier of the premises in accordance with
the provisions of section 47 of the Act.
Jika Ketua Pengarah berjanji untuk membersihkan atau mengurangkan sebarang tumpahan
atau pelepasan tidak sengaja, dia hendaklah menentukan kos penuh dan perbelanjaan
yang ditanggung dan boleh mendapatkan semula kos dan perbelanjaan tersebut daripada
pemilik atau penghuni premis itu mengikut peruntukan seksyen 47 Akta .
Jika Ketua Pengarah berjanji untuk membersihkan atau mengurangkan sebarang tumpahan atau pelepasan tidak sengaja, dia hendaklah menentukan kos penuh dan perbelanjaan yang ditanggung dan boleh mendapatkan semula kos dan perbelanjaan tersebut daripada pemilik atau
penghuni premis itu mengikut peruntukan seksyen 47 Akta .

115. LANGKAH-LANGKAH
KAWALAN RISIKO BAHAN
KIMIA BERBAHAYA KEPADA
KESIHATAN

116. HIERARKI KAWALAN RISIKO
PPE

117. PRINCIPLES OF CHEMICAL
HAZARD RISK CONTROL
Chemical Safety Management

118. DESIGN OF ENGINEERING CONTROL
EQUIPMENT

119. DESIGN OF ENGINEERING CONTROL
EQUIPMENT

120. ENGINEERING CONTROL
EQUIPMENT

121. ELEMEN KONSEP
‘CRADLE TO GRAVE’
•1
Pembelian
Penerimaan &
Penyimpanan
•2
•3
Penggunaan
•4
Perlupusan

122. PURCHASE OF CHEMICALS

123. PENERIMAAN BAHAN KIMIA

125. RE-LABELING OF CHEMICALS

126. •
CHEMICAL REGISTRATION

127. CHEMICAL REGISTRATION EXAMPLE

128. CHEMICAL STORAGE

129. PAPAN TANDA STOR
PENYIMPANAN
BAHAN KIMIA

130. CHEMICAL STORAGE STORE SIGN

132. CHEMICAL USE LOCATION
WARNING SIGNS
KAWASAN
PENGGUNAAN
BAHAN KIMIA
BERBAHAYA
KEPADA
KESIHATAN

133. CHEMICAL LEAK CONTROL
EMERGENCY EQUIPMENT

134. PROCEDURES FOR THE SAFE USE OF
CHEMICALS
SAFE PRACTICES WHEN HANDLING
CHEMICALS

135. SAFE PRACTICES WHEN HANDLING
CHEMICALS

136. SAFE PRACTICES WHEN HANDLING
CHEMICALS

137. SAFE PRACTICES WHEN HANDLING
CHEMICALS

138. PERSONAL PROTECTION EQUIPMENT

139. PERSONAL PROTECTION EQUIPMENT

140. Safety helmet / bump cap
Safety goggles face shield
EXAMPLE OF PERSONAL PROTECTIVE
EQUIPMENT (PPE)

141. Air purifying respirator.
Supplied air respirator
EXAMPLE OF PERSONAL PROTECTIVE
EQUIPMENT (PPE)

142. Long-sleeve shirt, apron, chemical suit.
Chemical resistance gloves,
finger coats
EXAMPLE OF PERSONAL PROTECTIVE
EQUIPMENT (PPE)

143. Safety shoes, safety boot
EXAMPLE OF PERSONAL PROTECTIVE
EQUIPMENT (PPE)

144. EMERGENCY ACTION EXPOSURE

145. EMERGENCY ACTION EXPOSURE

146. EMERGENCY ACTION EXPOSURE

147. LIQUID CHEMICAL SPILL
EMERGENCY ACTIONS

148. CHEMICAL WASTE DISPOSAL
PROCESS

149. PENALTI MAJIKAN
Denda RM 10,000
atau
Penjara 1 tahun
atau
Kedua-duanya