Hawaii Administrative Rules
Title 12 - DEPARTMENT OF LABOR AND INDUSTRIAL RELATIONS
Subtitle 8 - HAWAII OCCUPATIONAL SAFETY AND HEALTH DIVISION
Part 10 - BOILER AND PRESSURE VESSEL
Chapter 224.1 - PRESSURE VESSELS
Section 12-224.1-5 - Technical installation requirements
Universal Citation: HI Admin Rules 12-224.1-5
Current through August, 2024
(a) All pressure vessels shall be installed as required in section 12-220-2.1 and this chapter. An application for installation permit shall be submitted to the department prior to the commencement of work. Pressure vessels installed without an installation permit may be subject to citations with penalties up to $10,000 per day pursuant to section 12-220-22.
(b) First acceptance inspection and certification. The following shall apply to first acceptance inspections and certifications:
(1) Upon completion of the
installation, the contractor or owner shall arrange for acceptance inspection
with the department;
(2) The
installing contractor shall operationally test the pressure vessel controls and
safety devices prior to scheduling first acceptance inspection with the
department;
(3) The chief boiler
inspector or designated deputy inspector shall conduct the first data
inspection, acceptance inspection, and apply the required state pressure vessel
identification marking; and
(4) The
installing contractor shall test the pressure vessel as directed and witnessed
by the chief boiler inspector or designated deputy inspector.
(c) Clearances. All pressure vessel installations must allow sufficient clearance for normal operation, maintenance, and inspection (internal and external). Except as otherwise authorized by the department, clearances for pressure vessels shall not be less than three (3) feet where inspection openings are provided. Vessels having manholes shall have five (5) feet clearance from the manhole opening and any wall, ceiling, or piping that may prevent a person from entering. All other sides shall not be less than eighteen (18) inches between the vessel and adjacent walls or other structures. Alternative clearances in accordance with the manufacturer's recommendations are subject to acceptance by the department.
(d) Pressure relief devices. All pressure vessels shall be protected by pressure relief devices in accordance with the following requirements:
(1) Device requirements:
(A) Each pressure vessel shall be provided
with pressure relief devices, to protect against overpressure. These pressure
relief devices shall bear the National Board "NB" symbols, the ASME
certification mark, and the appropriate designator, as required by the ASME
BPVC;
(B) Deadweight or weighted
lever pressure relief valves shall not be used;
(C) An unfired steam boiler shall be equipped
with pressure relief valves as required in NBIC Part 1, 2.9;
(D) Pressure relief devices shall be selected
(e.g., material, pressure, etc.) and installed such that their proper
functioning will not be hindered by the nature of the vessel's contents;
and
(E) Relief valves, safety
valves, or safety relief valves shall be of the hand lift lever type whenever
possible to facilitate actuating and testing the device for free
operation;
(2) Number of
devices. At least one device shall be provided for protection of a pressure
vessel. Pressure vessels with multiple chambers with different maximum
allowable working pressures shall have a pressure relief device to protect each
chamber under the most severe coincident conditions;
(3) Location. The following shall apply to
location of devices:
(A) The pressure relief
device shall be installed directly on the pressure vessel, unless the source of
pressure is external to the vessel and is under such positive control that the
pressure cannot exceed the maximum overpressure permitted by the original code
of construction and the pressure relief device cannot be isolated from the
vessel, except as permitted by NBIC Part 1, 4.5.6(e)(2);
(B) Pressure relief devices intended for use
in compressible fluid service shall be connected to the vessel in the vapor
space above any contained liquid or in the piping system connected to the vapor
space; and
(C) Pressure relief
devices intended for use in liquid service shall be connected below the normal
liquid line. The liquid level during upset conditions shall be
considered;
(4) Capacity.
The following shall apply to the capacity of pressure relief devices:
(A) The pressure relief device(s) shall have
sufficient capacity to ensure that the pressure vessel is not exposed to
pressure greater than that specified in the original code of
construction;
(B) Vessels connected
by a system of piping not containing valves that can isolate any pressure
vessel shall be considered as one unit when determining capacity
requirements;
(C) Heat exchangers
and similar vessels shall be protected with a pressure relief device of
sufficient capacity to avoid overpressure in case of internal failure;
and
(D) The owner shall make
information regarding the basis of pressure relief device selection, including
required capacity, available to the jurisdiction;
(5) Set pressure. The following shall apply
to the set pressure of pressure relief devices:
(A) When a single pressure relief device is
used, the set pressure marked on the device shall not exceed the maximum
allowable working pressure; and
(B)
When more than one pressure relief device is provided to obtain the required
capacity, only one pressure relief device set pressure needs to be at the
maximum allowable working pressure. The set pressures of the additional
pressure relief devices shall be such that the pressure cannot exceed the
overpressure permitted by the code of construction; and
(6) Installation and discharge piping
requirements. The following shall apply to the installation and discharge
piping of pressure relief devices:
(A) The
opening through all pipe and fittings between a pressure vessel and its
pressure relief device shall have at least the area of the pressure relief
device inlet. The characteristics of this upstream system shall be such that
the pressure drop will not reduce the relieving capacity below that required or
adversely affect the proper operation of the pressure relief device. When a
discharge pipe is used, the size shall be such that any pressure that may exist
or develop will not reduce the relieving capacity below that required or
adversely affect the proper operation of the pressure relief device. It shall
be as short and straight as possible and arranged to avoid undue stress on the
pressure relief device;
(B) The
opening in the pressure vessel wall shall be designed to provide unobstructed
flow between the vessel and its pressure relief device;
(C) When two or more required pressure relief
devices are placed on one connection, the inlet cross-sectional area of this
connection shall be sized either to avoid restricting flow to the pressure
relief devices or made at least equal to the combined inlet areas of the
pressure relief devices connected to it. The flow characteristics of the
upstream system shall satisfy the requirements of NBIC Part 1, 4.5.6(e);
and
(D) There shall be no
intervening stop valves between the vessel and its pressure relief device(s),
or between the pressure relief device(s) and the point of discharge, except
under the following conditions:
(i) When these
stop valves are so constructed or positively controlled that the closing of the
maximum number of block valves at one time will not reduce the pressure
relieving capacity below the required relieving capacity;
(ii) Upon specific acceptance of the
jurisdiction, when necessary for the continuous operation of processing
equipment of such a complex nature that shutdown of any part is not feasible, a
full area stop valve between a pressure vessel and its pressure relief device
shall be provided for inspection and repair purposes only. This stop valve
shall be arranged so that it can be locked or sealed open, and it shall not be
closed except by an authorized person who shall remain stationed there during
that period of operation while the valve remains closed. The valve shall be
locked or sealed in the open position before the authorized person leaves the
station;
(iii) A full area stop
valve shall also be placed on the discharge side of a pressure relief device
when its discharge is connected to a common header for pressure relief devices
to prevent discharges from these other devices from flowing back to the first
device during inspection and repair. This stop valve shall be arranged so that
it can be locked or sealed open, and it shall not be closed except by an
authorized person who shall remain stationed there during that period of
operation while the valve remains closed. The valve shall be locked and sealed
in the open position before the authorized person leaves the station. This
valve shall only be used when a stop valve on the inlet side of the pressure
relief device is first closed;
(iv)
A pressure vessel in a system where the pressure originates from an outside
source shall have a stop valve between the vessel and the pressure relief
device, and this valve need not be sealed open, provided it also closes off
that vessel from the source of the pressure;
(v) Pressure relief device discharges shall
be arranged such that they are not a hazard to personnel or other equipment
and, when necessary, lead to a safe location for disposal of fluids being
relieved;
(vi) Discharge lines from
pressure relief devices shall be designed to facilitate drainage or be fitted
with drains to prevent liquid from collecting in the discharge side of a
pressure relief device. The size of discharge lines shall be such that any
pressure that may exist or develop will not reduce the relieving capacity of
the pressure relief device or adversely affect the operation of the pressure
relief device. It shall be as short and straight as possible and arranged to
avoid undue stress on the pressure relief device; and
(vii) Pressure vessel pressure relief devices
and discharge piping shall be safely supported. The reaction forces due to
discharge of pressure relief devices shall be considered in the design of the
inlet and discharge piping. Design of supports, foundations, and settings shall
consider vibration (including seismic when necessary), movement (including
thermal movement), and loadings (including reaction forces during device
operation) in accordance with jurisdictional requirements, manufacturer's
recommendations, and/or other industry standards, as
applicable.
(e) Supports. Each pressure vessel shall be safely supported. The potential for future hydrostatic pressure tests of the vessel after installation shall be considered when designing vessel supports. Design of supports, foundations, and settings shall consider vibration (including seismic and wind loads where necessary), movement (including thermal movement), and loadings (including the weight of water during a hydrostatic test) in accordance with jurisdictional requirements, manufacturer's recommendations, and other industry standards, as applicable.
(f) Piping. Piping loads on the vessel nozzles shall be considered. Piping loads include weight of the pipe, weight of the contents of the pipe, and expansion of the pipe from temperature and pressure changes (wind and seismic loads). The effects of piping vibration on the vessel nozzles shall also be considered.
(g) Bolting. All mechanical joints and connections shall conform to the manufacturers' installation instructions and recognized standards acceptable to the jurisdiction.
(h) Instruments and controls. The following shall apply to the instruments and controls of pressure vessels:
(1) Level indicating devices of steam drums
of unfired steam boilers shall be provided with two level indicating devices.
Direct level indicating devices shall be connected to a single water column or
connected directly to the drum, and the connections and pipe shall be not less
than NPS 1/2 (DN 15). Indirect level indicating devices acceptable to the
jurisdiction may be used; and
(2)
The pressure indicating devices of each pressure vessel, or system of pressure
vessels with no intervening valves, shall be equipped with a pressure gage
graduated to not less than one and a half (1-1/2) times nor more than three (3)
times the pressure which the safety or safety relief valve is set.
(i) Isolating valves. Each pressure vessel or multiple pressure vessels connected in series shall have isolating valves which isolate the vessel or vessels from the system in which it or they are installed.
(j) Additional requirements for compressed air vessels. The following shall apply to compressed air vessels:
(1) Under no
circumstances shall an air receiver be buried underground or located in an
inaccessible place;
(2) Belt guards
shall be installed on air compressor units fitted with drive belts;
(3) Drain pipe and valve shall be installed
at the lowest point of every pressure vessel subject to internal corrosion to
provide for draining or the removal of accumulated oil and water from an air
receiver. Adequate automatic traps may be installed in addition to drain
valves. The drain valve on an air receiver shall be opened and drained
frequently at such intervals as to prevent the accumulation of excessive
amounts of liquids in the receiver; and
(4) The use of thermoplastic piping, known as
PVC piping, to transport compressed air or other compressed gases, or the
testing of this piping with compressed air or other compressed gases, in
exposed above ground locations is prohibited. All thermoplastic piping used to
transport compressed air or other compressed gases shall be buried underground
or encased in shatter-resistant materials. In designing a thermoplastic piping
system to transport compressed air or other compressed gases, the strength at
the operating temperature, the pressure, the energetics, and specific failure
mechanisms shall be evaluated.
(k) Additional requirements for hot water storage tanks. The following shall apply to hot water storage tanks:
(1) Safety relief devices. Each hot water
storage tank shall be equipped with an ASME/NB certified temperature and
pressure relieving device set at a pressure not to exceed the maximum allowable
working pressure and 210 degrees Fahrenheit or the maximum allowable working
temperature of the vessel as designed. The temperature and pressure relieving
device shall meet the requirements of NBIC Part 1 4.5;
(2) Hot water storage tanks greater than 160
Psi maximum allowable working pressure shall be equipped with an ASME/NB
certified temperature and pressure relieving device set at a pressure not to
exceed the maximum allowable working pressure and 210 degrees Fahrenheit. In
lieu of this requirement, such tanks may be equipped with incompressible fluid
pressure rated relief valves with appropriate relieving capacity provided the
hot water system is installed with an over-temperature protection that
adequately prevent the generation of hot water in excess of 210 degrees
Fahrenheit; and acceptable to the jurisdiction; Examples of system
over-temperature protection:
(A) Operating
temperature control and high temperature limit switch with manual reset
installed at the potential source;
(B) Automatic self-adjusting over-temperature
protection;
(C) Tempering and
mixing valves;
(D) Solenoid
operated dump valves with thermostat probe rated for 210 degrees Fahrenheit
maximum scale range setting; and
(E) Any other system of over-temperature
protection controls to be demonstrated to function as designed and approved by
the jurisdiction;
(3)
Clearances. In addition to the clearance requirements under section 12-224.1-5
(c), each hot water storage tank shall have at least twelve (12) inches bottom
clearance;
(4) Each hot water
storage tank shall have a thermometer so located that it shall be easily
readable at or near the outlet. The thermometer shall be so located that it
shall at all times indicate the temperature of the water in the storage tank;
and
(5) Shut off valves. Each hot
water storage tank shall be equipped with stop valves in the water inlet piping
and the outlet piping for the hot water storage tank to be removed from service
without having to drain the complete system. Each hot water storage tank also
shall be equipped with a bottom drain valve to provide for flushing and
draining of the vessel.
(l) Additional requirements for pressure relief valves for steam to hot-water supply heat exchangers. When a hot-water supply is heated indirectly by steam in a coil or pipe within the service limitations set forth in the NBIC, the pressure of the steam used shall not exceed the safe working pressure of the hot water tank, and a safety relief valve of at least NPS 1 set to relieve at or below the maximum allowable working pressure of the tank, shall be applied on the tank.
(m) Description and concerns of specific types of pressure vessels.
(1) Compressed air
vessels. The following applies to compressed air vessels:
(A) Considerations of concern include
temperature variances, pressure limitations, vibration, and condensation. Drain
connections shall be verified to be free of any foreign material that may cause
plugging; and
(B) Inspections of
compressed air vessels shall consist of the following:
(i) Welds. Inspect all welds for cracking or
gouging, corrosion, and erosion. Particular attention shall be given to the
welds that attach brackets supporting the compressor. These welds may fail due
to vibration;
(ii) Shells and
heads: externally, inspect the base material for environmental deterioration
and impacts from objects. Hot spots and bulges are signs of overheating and
shall be noted and evaluated for acceptability. Particular attention shall be
paid to the lower half of the vessel for corrosion and leakage. For vessels
with manways or inspection openings, an internal inspection shall be performed
for corrosion, erosion, pitting, excessive deposit buildup, and leakage around
inspection openings. Ultrasonic thickness testing (UT) may be used where
internal inspection access is limited or to determine actual thickness when
corrosion is suspected;
(iii)
Fittings and attachments. Inspect all fittings and attachments for alignment,
support, deterioration, damage, and leakage around threaded joints. Any
internal attachments such as supports, brackets, or rings shall be visually
examined for wear, corrosion, erosion, and cracks;
(iv) Operation. Check the vessel nameplate to
determine the maximum allowed working pressure and temperature of the vessel.
Ensure the set pressure of the safety valve does not exceed that allowed on the
vessel nameplate and determine that the capacity of the safety valve is greater
than the capacity of the compressor. Ensure there is a functioning manual or
automatic condensate drain; and
(iv) Quick closure attachments. Filter-type
vessels usually have one quick-type closure head for making filter changes, see
NBIC Part 2, 2.3.6.5;
(2) The following shall apply to pressure
vessels with quick-actuating closures:
(A)
Due to the many different designs of quick-actuating closures, potential
failures of components that are not specifically covered shall be considered.
The scope of inspection shall include areas affected by abuse or lack of
maintenance and a check for inoperable or bypassed safety and warning
devices;
(B) Temperatures above
that for which the quick-actuating closure was designed can have an adverse
effect on the safe operation of the device. If parts are found damaged and
excessive temperatures are suspected as the cause, the operating temperatures
may have exceeded those temperatures recommended by the manufacturer. Rapid
fluctuations in temperatures due to rapid start-up and shutdown may lead to
cracks or yielding caused by excessive warping and high thermal stress. A
careful observation shall be made of the condition of the complete
installation, including maintenance and operation, as a guide in forming an
opinion of the care the equipment receives. The history of the vessel shall be
established, including: year built, materials of construction, extent of post
weld heat treatment, previous inspection results, and repairs or alterations
performed. Any leak shall be thoroughly investigated and the necessary
corrective action initiated;
(C)
Inspection of parts and appurtenances. Seating surfaces of the closure device,
including but not limited to the gaskets, 0-rings, or any mechanical
appurtenance to ensure proper alignment of the closure to the seating surface,
shall be inspected. This inspection can be made by using powdered chalk or any
substance that will indicate that the closure is properly striking the seating
surface of the vessel flange. If this method is used, a check shall be made to
ensure that:
(i) Material used shall not
contaminate the gasket or material with which it comes into contact;
and
(ii) The substance used shall
be completely removed after the examination;
(D) The closure mechanism of the device shall
be inspected for freedom of movement and proper contact with the locking
elements. This inspection shall indicate that the movable portions of the
locking mechanism are striking the locking element in such a manner that full
stroke can be obtained. Inspection shall be made to ensure that the seating
surface of the locking mechanism is free of metal burrs and deep scars, which
would indicate misalignment or improper operation. A check shall be made for
proper alignment of the door hinge mechanisms to ensure that adjustment screws
and locking nuts are properly secured. When deficiencies are noted, the
following corrective actions shall be initiated:
(i) If any deterioration of the gasket,
O-ring, etc., is found, the gasket, 0-ring, etc., shall be replaced
immediately. Replacements shall be in accordance with the vessel manufacturer's
specifications;
(ii) If any
cracking or excessive wear is discovered on the closing mechanism, the owner or
user shall contact the original manufacturer of the device for spare parts or
repair information. If this cannot be accomplished, the owner or user shall
contact an organization competent in quick-actuating closure design and
construction prior to implementing any repairs;
(iii) Defective safety or warning devices
shall be repaired or replaced prior to further operation of the
vessel;
(iv) Deflections, wear, or
warping of the sealing surfaces may cause out-of-roundness and misalignment.
The manufacturer of the closure shall be contacted for acceptable tolerances
for out-of-roundness and deflection; and
(v) The operation of the closure device
through its normal operating cycle shall be observed while under control of the
operator. This shall indicate if the operator is following posted procedures
and if the operating procedures for the vessel are adequate;
(E) Gages, safety devices, and
controls. The required pressure gage shall be installed so that it is visible
from the operating area and located in such a way that the operator can
accurately determine the pressure in the vessel while it is in operation. The
gage dial size shall be of such a diameter that it can be easily read by the
operator. This gage shall have a pressure range of at least one and a half
(1.5) times, but not more than four (4) times, the operating pressure of the
vessel. There shall be no intervening valve between the vessel and
gage;
(F) The pressure gage shall
be of a type that will give accurate readings, especially when there is a rapid
change in pressure. It shall be of rugged construction and capable of
withstanding severe service conditions. Where necessary, the gage shall be
protected by a siphon or trap;
(G)
Pressure gages intended to measure the operating pressure in the vessel are not
usually sensitive or easily read at low pressures approaching atmospheric. It
may be advisable to install an auxiliary gage that reads inches of water and is
intended to measure pressure from atmospheric through low pressures. This
ensures that there is zero pressure in the vessel before opening. It would be
necessary to protect the auxiliary low-pressure gage from the higher operating
pressures;
(H) Provisions shall be
made to calibrate pressure gages or to have them checked against a master gage
as frequently as necessary;
(I) A
check shall be made to ensure that the closure and its holding elements must be
fully engaged in their intended operating position before pressure can be
applied to the vessel. A safety interlock device shall be provided that
prevents the opening mechanism from operating unless the vessel is completely
depressurized; and
(J)
Quick-actuating closures held in position by manually operated locking devices
or mechanisms, and which are subject to leakage of the vessel contents prior to
disengagement of the locking elements and release of the closure, shall be
provided with an audible and/or visible warning device to warn the operator if
pressure is applied to the vessel before the closure and its holding elements
are fully engaged, and to warn the operator if an attempt is made to operate
the locking device before the pressure within the vessel is released. Pressure
tending to force the closure clear of the vessel must be released before the
closure can be opened for access; and
(3) Inspection of Pressure Vessels for Human
Occupancy (PVHOs). The following shall apply to the inspection of PVHOs:
(A) General and operational. PVHOs shall be
constructed in accordance with ASME PVHO-1. This code adopts ASME BPV Section
VIII and therefore the vessels shall bear a "U" or "U2" ASME designator.
Inspections should be conducted using ASME PVHO-2 for reference;
(B) Cast and ductile iron fittings are not
allowed;
(C) Due to the human
occupancy element, a person shall be in attendance to monitor the PVHO when in
operation, in the event there is an accident;
(D) The installation shall be such that there
is adequate clearance to inspect it properly. In some applications, such as
underground tunneling, it may be impossible to perform a complete external
inspection;
(E) Internal
inspection. Where existing openings permit, perform a visual internal
inspection of the vessel. Look for any obvious cracks and note areas that are
subject to high stress such as welds, welded repairs, head-to-shell
transitions, sharp interior corners, and interior surfaces opposite external
attachments or supports. The vessel shall be free of corrosion, damage, dents,
gouges, or other damage. All openings leading to external fittings or controls
shall be free from obstruction. All exhaust inlets shall be checked to prevent
a chamber occupant from inadvertently blocking the opening;
(F) External inspection. The inspector shall
closely examine the external condition of the pressure vessel for corrosion,
damage, dents, gouges, or other damage. The lower half and the bottom portions
of insulated vessels shall receive special focus, as condensation or moisture
may gravitate down the vessel shell and soak into the insulation, keeping it
moist for long periods of time. Penetration locations in the insulation or
fireproofing such as saddle supports, sphere support legs, nozzles, or fittings
shall be examined closely for potential moisture ingress paths. When moisture
penetrates the insulation, the insulation may actually work in reverse, holding
moisture in the insulation or near the vessel shell. Insulated vessels that are
run on an intermittent basis or that have been out of service require close
scrutiny. In general, a visual inspection of the vessel's insulated surfaces
shall be conducted once per year. The most common and superior method to
inspect for suspected corrosion under insulation (GUI) damage is to completely
or partially remove the insulation for visual inspection. The method most
commionly utilized to inspect for GUI without insulation removal is by X-ray
and isotope radiography (film or digital), or by real time radiography,
utilizing imaging scopes and surface profilers. The real-time imaging tools
will work well if the vessel geometry and insulation thickness allows. Other
less common methods to detect GUI include specialized electromagnetic methods
(pulsed eddy current and electromagnetic waves) and long-range ultrasonic
techniques (guided waves). There are also several methods to detect moisture
soaked insulation, which is often the beginning for potential GUI damage.
Moisture probe detectors, neutron backscatter, and thermography are tools that
can be used for GUI moisture screening. Proper surface treatment (coating) of
the vessel external shell and maintaining weather-tight external insulation are
the keys to prevention of GUI damage;
(G) Inspection of parts and appurtenances
(e.g., piping systems, pressure gage, bottom drain). As stated above, cast iron
is not allowed on PVHOs and shall be replaced with parts fabricated with other
suitable materials, in accordance with ASME BPVG Section II. If valves or
fittings are in place, check to ensure that these are complete and functional.
The inspector shall note the pressure indicated by the gage and compare it with
other gages on the same system. If the pressure gage is not mounted on the
vessel itself, it shall be ascertained that the gage is installed on the system
in such a manner that it correctly indicates actual pressure in the vessel. The
inspector shall verify that the vessel is provided with a drain opening. The
system shall have a pressure gage designed for at least the most severe
condition of coincident pressure in normal operation. This gage shall be
clearly visible to the person adjusting the setting of the pressure control
valve. The graduation on the pressure gage shall be graduated to not less than
one and a half (1.5) times the maximum allowable working pressure (MAWP) of the
vessel. Provisions shall be made to calibrate pressure gages or to have them
checked against a standard test gage. Any vents and exhausts shall be piped at
least ten (10) feet from any air intake. Venting shall be provided at all high
points of the piping system;
(H)
Inspection of view ports and windows. Each window shall be individually
identified and be marked in accordance with PVHO-1. If there are any
penetrations through windows, they must be circular. Windows must be free of
crazing, cracks, and scratches. Windows and viewports have a maximum interval
for seat or seal inspection and refurbishment. Documentation shall be checked
to ensure compliance with PVHO-2, Table 2-4.3- 1, Table 2-4.3-2 (see Exhibit
1); and
(I) Inspection of pressure
relief devices. Pressure relief devices must have a quick opening manual
shutoff valve installed between the chamber and the pressure relief device,
with a frangible seal in place, within easy access to the operator. The
pressure relief device shall be constructed in accordance with ASME BPVC
Section VIII. The discharge from the pressure relief device must be piped
outside to a safe point of discharge. Rupture disks may be used only if they
are in series with a pressure relief valve, or when there is less than two (2)
cubic feet of water volume. Verify that the safety valve is periodically tested
either manually by raising the disk from the seat or by removing and testing
the valve on a test stand.
Disclaimer: These regulations may not be the most recent version. Hawaii may have more current or accurate information. We make no warranties or guarantees about the accuracy, completeness, or adequacy of the information contained on this site or the information linked to on the state site. Please check official sources.
This site is protected by reCAPTCHA and the Google
Privacy Policy and
Terms of Service apply.
