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SEMI F5-1101 © SEMI 1990 , 2001 3 may be as lo w as 10% ). Additio nal by-prod ucts will h a ve different an d so metimes m o re hazardous properties. 7.2 Considerable research h as been con ducted into various hazardous…

SEMI F5-1101 © SEMI 1990, 2001 2
4 Referenced Standards
4.1 SEMI Standards
SEMI S2 — Environmental, Health, and Safety
Guideline for Semiconductor Manufacturing Equipment
SEMI S5 — Safety Guideline for Flow Limiting
Devices
SEMI S8 — Safety Guidelines for Ergonomics
Engineering of Semiconductor Manufacturing
Equipment
4.2 Code of Federal Regulations — United States
Environmental Protection Agency
1
40 CFR Part 63 (Clean Air Act 112 (b)(1))
4.3 Uniform Codes
2
Uniform Fire Code — Article 80 — Hazardous
Material
NOTE 1: Unless otherwise indicated, all documents cited
shall be the latest published versions.
5 Terminology
5.1 Abbreviations and Acronyms
5.1.1 CVD — Chemical Vapor Deposition
5.1.2 EPI — epitaxial deposition
5.1.3 HAP — Hazardous Air Pollutants [as defined by
40 CFR Part 63 (Clean Air Act 112 (b)(1))
5.1.4 PFC — perfluorocompounds
5.1.5 POU — Point of use
5.1.6 VOC — Volatile Organic Compounds
5.2 Definitions
5.2.1 classification of emissions — understanding the
composition of process exhausts.
5.2.2 efficiency — the ratio (or fraction or proportion)
of removed chemical species to its input amount
5.2.3 End-of-Pipe Abatement — abatement
technologies that can be fitted at the discharge point of
the exhaust system.
5.2.4 flow capacity — the maximum flow any specific
equipment can handle.
5.2.5 occupational exposure limits (OELs) — for the
purpose of this document, OELs are generally
established on the basis of an eight-hour workday.
1 United States Government Code of Federal Regulations, free from
the web site at http://www.epa.gov
2 International Conference of Building Officials (ICBO), 5360
Workman Mill Road, Whittier, CA 90601-2298
Various terms are used to refer to OELs, such as
permissible exposure levels, Threshold Limit Values®,
maximum acceptable concentrations, maximum
exposure limits, and occupational exposure standards.
However, the criteria used in determining OELs can
differ among the various countries that have established
values. Refer to the national bodies responsible for the
establishment of OELs. (Threshold Limit Value is a
registered trademark of the American Conference of
Governmental Industrial Hygienists.)
5.2.6 Point-of-Use Abatement — abatement
technologies that can be fitted at the point of discharge
of the gaseous emission from semiconductor process
equipment. These devices are also called exhaust
conditioners.
5.2.7 removal capacity — amount of a species which
can be removed.
5.2.8 usage reduction — reducing the total volume of
process chemicals requiring abatement.
6 Philosophy
6.1 Gaseous mixtures potentially emitted from
numerous processes could also produce hazards within
exhaust ducts.
6.2 With increasing legal requirements worldwide on
both worker safety and general environmental
protection, more effective exhaust management is
required.
6.3 This demands a detailed understanding of the
chemical and physical properties of the chemical
compounds being emitted from processes, and of the
conditions under which they are released.
6.4 Careful design of the abatement systems is required
to attain both high efficiency and maximum economy.
7 Classification of Emissions
7.1 The following fundamental points regarding
exhaust emissions should be considered:
• Exhaust contaminants might be solely the material
used in the process (e.g., isopropyl alcohol (IPA)
from a rinse chamber)
• In plasma and thermal chambers many reactions
occur, both those desired and others; therefore by-
products are also key components of exhaust
emissions.
• In theory, most possible combinations of the
elements in the input gases may be found as
compounds in the exhaust. In practice, the main
components will be the unused process gas (the
percentage consumed in the process varies, and

SEMI F5-1101 © SEMI 1990, 20013
may be as low as 10%). Additional by-products
will have different and sometimes more hazardous
properties.
7.2 Considerable research has been conducted into
various hazardous by-products of processes, from
explosive solids to organochlorine compounds with
mutagenic properties. (See Sections 13.1 through
13.3.)
7.3 In considering selection of exhaust systems and
abatement technology, it is essential to review all the
materials likely to be present in the exhaust.
7.4 Contributions from the materials on the wafer must
also be considered, as they often cause blocked
exhausts (e.g., aluminum etches produce aluminum
chloride (a by-product of removal of aluminum from
the wafer with chlorinated gases)).
7.5 Processes that produce specific hazardous by-
products should be evaluated for appropriate point-of-
use abatement technology before discharge to an
exhaust system.
7.6 Gaseous and particulate contaminants emitted from
semiconductor manufacturing can be divided
conveniently into nine major groups, each of which
might justify its own exhaust system.
7.6.1 Group-1 Acid — Easily hydrolyzable acids, (e.g.,
hydrogen chloride hydrolyzes into hydrochloric acid.)
7.6.2 Group-2 Acid aerosols (“difficult–to-scrub”) —
This group includes acids that generate aerosols and
that are not easily removed by simple water scrubbers
(e.g., aqua regia, sulfuric and nitric).
NOTE 2: High concentrations of easily soluble acids will also
fall into the “difficult-to-scrub” category.
7.6.3 Group-3 Ammonia — Exhaust streams
containing ammonia
7.6.4 Group-4 Volatile Organic Compounds (VOCs)
— Exhausts containing volatile organic compound
vapors or flammable gas discharge requiring
destruction.
7.6.5 Group-5 Pyrophoric — Exhausts containing
pyrophoric gases.
7.6.6 Group-6 Emergency Release Discharges —
Enclosures are provided with additional exhausts to
contain sudden unanticipated releases of gas from
cylinders, etc.
7.6.7 Group-7 Special/Direct — Additional exhausts
used to keep specific gases separate for recovery
purposes (e.g., hydrogen (H
2
) reclamation from EPI or
PFC reclamation from CVD tools, Oxides of Nitrogen
(NO
x
)).
7.6.8 Group-8 General Exhaust Systems without End-
of-Pipe Treatment — Exhaust of heat or post-treatment
exhaust from POU abatement systems.
7.6.9 Group-9 Highly Toxic Gas Exhaust — Highly
toxic gases especially those with poor warning
properties (e.g., arsine, phosphine, diborane, germane).
The end user has a primary responsibility to prevent
discharge of these gases above a regulated level (e.g.,
usually one-half (1/2) of Immediately Dangerous to
Life and Health (IDLH) levels).
NOTE 3: Facility exhaust systems may be called by a number
of different names such as: Acid, Corrosive, Ammonia,
Scrubbed, VOC, Solvent, Incinerated, Highly Toxic, Toxic,
Dedicated, Special, PFC, General, Heat, Treated, or others.
The actual facility exhaust system name, and what groups are
routed to each system, will vary by factory and by country.
7.7 The groups listed in Section 7.6 are not a definitive
division, but represent a summation of common
industry practice for separation. The division is based
on three basic principles:
• avoiding mixing of incompatible gases in the
exhaust,
• potential need for different end-of-pipe abatement
technologies, and,
• keeping materials separate for recovery.
7.8 The number of separate exhaust systems used is
entirely a decision for each facility, based on the
following:
• processes and chemicals used,
• the number of each type of process,
• whether recovery of gases is required,
• whether point-of-use (POU) abatement is installed,
and
• compatibility of emissions with each other or the
effluent handling system.
7.9 In theory, if POU abatement systems are fitted to
all sources of gaseous effluent all exhaust could then be
combined into a single exhaust system.
7.9.1 In practice most facilities operate a compromise
between the two extremes with two to four separate
exhaust systems and point-of-use abatement systems
fitted only to certain sources. The decision (as to which
combination to use) will often be based on economic
and space constraints.
7.9.2 Safety and environmental factors listed below,
should always be considered first when determining
specific gaseous sources that require POU abatement
systems.

SEMI F5-1101 © SEMI 1990, 2001 4
7.10 Many types of process equipment use and exhaust
incompatible gases sequentially (e.g., silane and then
nitrogen trifluoride (NF
3
) as elements of a deposition
and cleaning cycle).
7.10.1 With more than one of these processes being
discharged asynchronously into a common exhaust
duct, undesired reactions may occur.
7.10.2 It is possible to avoid this problem by fitting the
equipment outlet with three-way valves to divert the
discharge to the correct exhaust system, depending on
equipment process step. Three-way valves may not be
necessary if pump ballast-gas flow is increased to dilute
gases.
7.10.2.1 Switching must accurately account for the gas
transmission times from process chamber inlet to the
exhaust valve.
7.10.2.2 Introduction of additional mechanical devices
could create major hazards, reliability, and service or
maintenance issues.
7.10.2.3 Valves must incorporate failsafe designs to
ensure pump outlet is not shut off.
7.10.3 An alternative solution is to fit a local POU
abatement system that treats at least one component and
is not adversely affected by the other components.
7.11 Point-of-Use (POU) Abatement Devices
7.11.1 POU abatement devices are designed to operate
at the process tool or pump outlet, and to remove
hazardous gases BEFORE they enter the exhaust
ductwork.
7.11.2 An end-of-pipe scrubber does not protect the
facility from reactions in the ductwork. Reactions
between process gases, as discussed above, or reactions
with other process by-products within the ductwork
itself are not prevented by end-of-pipe systems either.
7.11.3 POU abatement devices may be appropriate
wherever the exhaust gases can react in the ductwork.
7.11.4 If process systems are not treated with POU
abatement devices, the higher concentrations of
hazardous gases will present a higher risk during a leak
into the facility space.
7.11.5 Improperly functioning POU abatement devices
can create backpressure that can increase the risk of a
leak.
7.12 Four significant consequences can be foreseen
from effluent gas reactions in the ductwork:
7.12.1 Blocked Ducts — Reactions between gases, or
condensation of vapors, can produce solids and semi-
solids (such as crystals, slurries or gels) that will block
the ductwork.
7.12.1.1 Collection of solids can create dead leg
sections that may contain reactive byproducts or unused
raw materials. Catastrophic release of these trapped
materials could generate a significant hazard.
7.12.1.2 Extensive downtime (for clean out, or ducts
collapsing under the weight of accumulated solids) is a
possible undesirable outcome of this condition.
7.12.1.3 Solids deposited (such as from metal etching)
can, themselves, be both corrosive and hazardous,
leading to health risks for people performing cleaning
in ductwork. (See Related Documents 13.1 through
13.3).
7.12.1.4 Blocked ducts may result in toxic process
gases or by products escaping into the work area.
7.12.2 Duct Corrosion — Etching and some chamber
cleaning process emissions are corrosive. Both metallic
(including stainless steel) and plastic ducting can be
attacked, resulting in the release of hazardous gas or
condensed liquids into the workplace.
7.12.3 Duct Fires or Explosions — Flammable and
pyrophoric gases can ignite in the ductwork. If the
ductwork is combustible or has flammable or
combustible deposits in it (e.g., hydrocarbon pump oil),
facility fires can result.
7.12.4 Additional information on protection of
Industrial Exhaust systems from fires may be found in
FM Global Loss Prevention Data Sheet 7-78,
“Industrial Exhaust Systems”.
NOTE 4: Destruction of whole production lines with multi-
million dollar cost impact has resulted from such incidents.
7.12.5 Formation of Ammonium Compounds — If
ammonia is discharged into a duct with acid
compounds, a sub-micron ammonium compound fume
can be generated, that is not easily removed by end-of-
pipe systems.
7.12.5.1 The result is visible discharges.
7.12.5.2 Ammonium compounds produce solids in the
duct.
7.13 If any of the above reactions can occur in the
process exhaust, POU abatement should be considered.
7.14 Exhausts of oil-lubricated vacuum pumps should
be fitted with well-maintained oil mist separators/
filters.
7.15 POU abatement devices may also be needed
upstream of the recovery device for the recovery of
some gaseous compounds (e.g., hydrogen (H
2
), PFC
gases).