NAFTA: Specific Rules of Origin
List of Amendments to
NAFTA Annex 401
January 1, 2003
NAFTA Annex 401 (January 1,
2003)
Other versions of Annex 401
Alcoholic Beverages - Heading 22.03-22.09
Explanation: The new rules allow certain goods produced by mixing
small quantities of non-NAFTA alcoholic beverages with NAFTA originating
alcoholic beverages to qualify for NAFTA preferences.
New rules of origin:
22.03-22.07 |
A change to heading 22.03 through 22.07 from any
heading outside that group, except from tariff item 2106.90.ee or
heading 22.08 through 22.09. |
2208.20 |
A change to subheading 2208.20 from any other heading,
except from tariff item 2106.90.ee or heading 22.03 through 22.07 or
22.09. |
2208.30-2208.70 |
No required change in tariff classification to
subheading 2208.30 through 2208.70, provided that the non-originating
alcoholic ingredients constitute no more than 10 percent of the
alcoholic content of the good by volume. |
2208.90 |
A change to subheading 2208.90 from any other heading,
except from tariff item 2106.90.ee or heading 22.03 through 22.07 or
22.09. |
22.09 |
A change to heading 22.09 from any other heading,
except from tariff item 2106.90.ee or heading 22.03 through 22.08. |
Petroleum/Topped Crude - Heading 27.10-27.15
Explanation: The new rule of origin specifies a number of
processes which confers NAFTA origin and provides definitions of those
processes in a Chapter Note.
New rule of origin:
27.10 |
A change to heading 27.10 from any other heading,
except from heading 27.11 through 27.15; or
Production of any good of heading 27.10 as the result of atmospheric
distillation, vacuum distillation, catalytic hydroprocessing, catalytic
reforming, alkylation, catalytic cracking, thermal cracking, coking or
isomerization. |
27.11-27.15 |
A change to heading 27.11 through 27.15 from any
heading outside that group, except from heading 27.10. |
Chapter Note for Chapter 27:
Note: |
For the purposes of heading 27.10, the following
processes confer origin:
- Atmospheric distillation - A separation process in which
petroleum oils are converted, in a distillation tower, into fractions
according to boiling point and the vapor then condensed into different
liquefied fractions. Liquefied petroleum gas, naphtha, gasoline,
kerosene, diesel/heating oil, light gas oils, and lubricating oil are
produced from petroleum distillation;
- Vacuum distillation - Distillation at a pressure below
atmospheric but not so low that it would be classed as molecular
distillation. Vacuum distillation is useful for distilling
high-boiling and heat-sensitive materials such as heavy distillates in
petroleum oils to produce light to heavy vacuum gas oils and residuum.
In some refineries gas oils may be further processed into lubricating
oils;
- Catalytic hydroprocessing - The cracking and/or treating of
petroleum oils with hydrogen at high temperature and under pressure,
in the presence of special catalysts. Catalytic hydroprocessing
includes hydrocracking and hydrotreating;
- Reforming (catalytic reforming) - The rearrangment of
molecules in a naphtha boiling range material to form higher octane
aromatics (i.e., improved antiknock quality at the expense of gasoline
yield). A main product is catalytic reformate, a blend component for
gasoline. Hydrogen is another by-product;
- Alkylation - A process whereby a high-octane blending
component for gasolines is derived from catalytic combination of an
isoparaffin and an olefin;
- Cracking - A refining process involving decomposition and
molecular recombination of organic compounds, especially hydrocarbons
obtained by means of heat, to form molecules suitable for motor fuels,
monomers, petrochemicals, etc.:
- Thermal cracking - Exposes the distillate to temperatures of
approximately 540-650C (1000-1200F) for varying periods of time.
Process produces modest yields of gasoline and higher yields of
residual products for fuel oil blending,
- Catalytic cracking - Hydrocarbon vapors are passed at
approximately 400C (750F) over a metallic catalyst (e.g.,
silica-alumina or platinum); the complex recombinations (alkylation,
polymerization, isomerization, etc.) occur within seconds to yield
high-octane gasoline. Process yields less residual oils and light
gases than thermal cracking;
- Coking - A thermal cracking process for the conversion of
heavy low grade products, such as reduced crude, straight run pitch,
cracked tars, and shale oil into solid coke (carbon) and lower boiling
hydrocarbon products which are suitable as feed for other refinery
units for conversion into lighter products; and
- Isomerization - The refinery process of converting petroleum
compounds into their isomers.
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