Addendum #2 9-23-2026.pdf

Date Printed: Sep 23, 2026 Page: 1 FORM ID: WV-PRC-CRFQ-002 2020/05

Department of Administration Purchasing Division 2019 Washington Street East Post Office Box 50130 Charleston, WV 25305-0130

State of West Virginia Centralized Request for Quote

Construction

Proc Folder: 2029896 Reason for Modification:

Doc Description: Cacapon State Park New Sewage Lift Station Addendum #2 is issued to publish pre-bid sign in sheet, agency responses to all vendor submitted que..... See Page 2 for complete infoProc Type: Central Purchase Order

Date Issued Solicitation Closes Solicitation No Version

2026-09-23 2026-10-13 13:30 CRFQ 0310 DNR2700000003 3

BID RECEIVING LOCATION

BID CLERK

DEPARTMENT OF ADMINISTRATION

PURCHASING DIVISION

2019 WASHINGTON ST E

CHARLESTON WV 25305

US

VENDOR

Vendor Customer Code:

Vendor Name :

Address :

Street :

City :

State : Country : Zip :

Principal Contact :

Vendor Contact Phone: Extension:

FOR INFORMATION CONTACT THE BUYER

Joseph (Josh) E Hager III

(304) 558-2306 joseph.e.hageriii@wv.gov

Vendor Signature X FEIN# DATE

All offers subject to all terms and conditions contained in this solicitation

Date Printed: Sep 23, 2026 Page: 2 FORM ID: WV-PRC-CRFQ-002 2020/05

Reason for Modification:

Addendum #2 is issued to publish pre-bid sign in sheet, agency responses to all vendor submitted questions and extend bid close date.

ADDITIONAL INFORMATION

The West Virginia Purchasing Division is soliciting bids on behalf of Cacapon Resort State Park to establish a contract for installing a new Sewage Pump Lift Station at Cacapon State Park per the attached specifications and terms and conditions.

INVOICE TO SHIP TO

DIVISION OF NATURAL

RESOURCES

DIVISION OF NATURAL

RESOURCES

112 CALIFORNIA AVENUE CACAPON RESORT STATE

PARK

BLDG 4 818 CACAPON LODGE DR

CHARLESTON WV BERKELEY SPRINGS WV

US US

Line Comm Ln Desc Qty Unit Issue Unit Price Total Price 1 Heavy construction services

Comm Code Manufacturer Specification Model #

72121504

Extended Description:

Cacapon State Park Sewage Lift Station

SCHEDULE OF EVENTS

Line Event Event Date

Revised 6/8/2012

SOLICITATION NUMBER: [Insert RFQ, RFP No.] Addendum Number: [Insert Number]

The purpose of this addendum is to modify the solicitation identified as [insert RFQ, RFP No.] (“Solicitation”) to reflect the change(s) identified and described below.

Applicable Addendum Category:

[ ] Modify bid opening date and time

[ ] Modify specifications of product or service being sought

[ ] Attachment of vendor questions and responses

[ ] Attachment of pre-bid sign-in sheet

[ ] Correction of error

[ ] Other

Description of Modification to Solicitation:

Additional Documentation: Documentation related to this Addendum (if any) has been included herewith as Attachment A and is specifically incorporated herein by reference.

Terms and Conditions:

1. All provisions of the Solicitation and other addenda not modified herein shall remain in full force and effect.

2. Vendor should acknowledge receipt of all addenda issued for this Solicitation by completing an Addendum Acknowledgment, a copy of which is included herewith.

Failure to acknowledge addenda may result in bid disqualification. The addendum acknowledgement should be submitted with the bid to expedite document processing.

ATTACHMENT A

RFI: Vendor Questions for CRFQ DNR27*03 Cacapon Lift Station

Q1. The solicitation documents specify a packaged duplex grinder pump station capable of providing 44 GPM at 87' TDH. Given the limitation imposed by the 87' TDH requirement, will 2 HP grinder pumps rated at 31 GPM at 87' TDH be acceptable?

A. Yes, 2hp grinder pumps rated at 31 GPM is acceptable. Since the desired flowrate is now 31 GPM, the new Total Dynamic Head (TDH) for the system is 65 ft. (with only 5ft. of static head/elevation change). Also, due to existing electrical capacity of 20A feed circuit, the controller will need to be designed to only allow 1 pump to run at a time or have a delayed start of the lag pump. (See attached Supplementary Specifications.)

Q2. The existing electrical feed is served by a 3-pole, 20A breaker labeled 230V, 3-phase. Please confirm whether the actual voltage at the existing pump station control panel is 230V or 208V.

A. The control panel is 208V.

Q3. Specification Sections 1.01 (Scope of Work) and 2.01 (Polyethylene Wetwell/Drywell) both reference a NEMA 6P electrical quick disconnect (EQD). Will a NEMA 6-rated junction box for float and pump cable connections be acceptable in lieu of the specified EQD disconnects?

A. Junction Box should bean above ground NEMA 4X located adjacent to the control panel.

(See attached Supplementary Specifications.)

Q4. Specification Section 2.01 (Polyethylene Wetwell/Drywell) requires double-wall construction. Will a single-wall fiberglass packaged pump station be acceptable in lieu of the specified double-wall construction?

A. Yes, single-wall fiberglass is acceptable.

Q5. Specification Section 2.01 (Polyethylene Wetwell/Drywell) lists a tank capacity of 36" x 96".

Given the lower flow rate associated with the proposed pumps, will a 48" x 96" tank be acceptable as an alternative to provide additional wastewater storage capacity?

A. Yes, use 48-inch X 96-inch for the Wetwell/Drywell. (See attached Supplementary Specifications.)

Q6. Specification Section 2.01 (Polyethylene Wetwell/Drywell) specifies tank internal piping and hardware rated for 150 PSI working pressure. Will the manufacturer's factory-standard check and isolation valves be acceptable?

A. Yes, the manufacturer’s factory-standard check and isolation valves will be acceptable.

Q7. Specification Section 2.02 (Pump) specifies a progressing cavity type pump. Will centrifugal wastewater grinder pumps be acceptable in lieu of progressive cavity grinder pumps?

A. Yes, use 2hp centrifugal wastewater grinder pumps as shown in attached Supplementary Specifications.

Q8. Specification Section 2.02 (Pump) specifies a 3 HP minimum. Will 2 HP pumps be acceptable?

A 3 HP pump will not operate on the existing electrical feed or breaker and will not achieve the specified 44 GPM at 87' TDH.

A. Yes, use 2hp pumps as shown in attached Supplementary Specifications.

Q9. Specification Section 2.03 (Grinder) lists performance details including 4 FPS, an inlet shroud, and 1,800 RPM that do not correspond to a centrifugal grinder pump configuration. Will the manufacturer's standard limitations for 2 HP grinder pumps be an acceptable alternative?

A. Yes, use the manufacturer’s standard limitations for 2hp grinder pumps.

Q10. Specification Section 2.04 (Electric Motor) specifies a 230V, 3-phase pump with an estimated 10.5A full load current per pump. The existing feed breaker is rated 20A at 230V, and the existing pumps draw 7A each. Will the feed breaker be upsized to accommodate a duplex station drawing approximately 10A per pump at 230V?

A. No, the feed breaker will not be upsized. The controller will need to be designed to only allow 1 pump to run at a time or have a delayed start of the lag pump. (See attached Supplementary Specifications.)

Q11. Specification Section 2.06 (Check Valve) requires a continuous operating pressure rating of 235 PSI and states that ball checks are not acceptable. Will an exception be granted for factory-packaged grinder pump stations utilizing lift-out check valves on the pump base assembly, such as the SRA125CV used with Pentair grinder pump packages?

A. Yes, manufacturer’s factory standard is acceptable for check valves and ball checks.

Q12. Specification Section 2.08 lists core components associated with progressive cavity pumps.

Will submersible centrifugal grinder pumps operating on a stainless steel guide rail system be an acceptable alternative in lieu of the specified progressive cavity system?

A. Yes, use submersible centrifugal grinder pumps. (See attached Supplementary Specifications.)

Q13. Specification Section 2.09 (Controls) specifies pressure switch operation. Will a four-float control system housed in a NEMA 4, non-metallic or stainless steel enclosure be acceptable in lieu of pressure switch operation?

A. Yes.

Clarification:

A WV Certified Septic Sewage Installer certificate will be required only if the vendor encounters sewage liquids that need pumped from the old lift station.

Supplementary Specifications - CRFQ DNR27*03

PART 1 - GENERAL

1.1 PERFORMANCE REQUIREMENTS

Contractor shall furnish and install (1) Grinder Packaged duplex pumping station 2hp Myers VS20 or engineer’s pre-approved equal. Each submersible centrifugal grinder pump shall be capable of meeting the following performance requirements:

65’ HEAD 31 GPM FLOW

Note: Due to limitations of the existing electrical 20A feed circuit, the controller will need to be designed to only allow 1 pump to run at a time or have a delayed start of the lag pump.

PART 2 – PUMPING SYSTEM

2.1 PUMPS

The grinder pump(s) shall be manufactured in the United States utilizing domestic parts and components in its construction. The volute, seal plate, cord cap and motor housing shall be constructed of high-quality ASTM Class 30 minimum cast iron. The pump(s) shall be painted with air dry enamel. All exposed hardware shall be 300 series stainless steel. Discharge connection shall be a standard 1.25-inch NPT in the vertical position.

The pump impeller shall be of the recessed, vortex design. The impeller shall be of stainless-steel construction and machined for threading to the motor shaft. The impeller shall be capable of being trimmed to meet specific performance characteristics.

An upper single row ball radial bearing and a lower double row angular contact bearing shall be provided. Bearings shall be permanently lubricated by the dielectric oil that fills the motor housing. The shaft shall be machined from solid 400 series stainless steel and be designed with large diameters and minimum overhang to reduce shaft deflection and prolong bearing and seal life

The motor shaft shall be of 416 stainless steel.

2.2 GRINDER

The stationary cutter shall be circular in design and contain evenly spaced cutting slots that extend outwards from the inlet of the pump. The slots are tapered inward toward the inlet to help direct slurry through the cutting slots into the pump. The slots are to be angled, or undercut, to help maintain a sharp axial cutting edge, even as the axial face wears during use. The stationary cutter shall be pressed into the suction opening of the volute and held in place by four 300 series stainless steel screws. The stationary cutter shall be provided with tapped back-off holes so that screws can be used to remove the cutter from the volute. The rotating cutter shall contain three axial cutting arms extending from the hub, perpendicular to the pump shaft, that are shaped to aid in the rejection of suspended debris that has not been sufficiently reduced in size by the axial cutting action.

The curved, leading edge of the cutting arms shall create a scissor action with the cutting slots of the stationary cutter plate to minimize the required torque. This will allow the cutter to macerate tough objects and prolong cutter life. Serrations on the hub of the cutter add additional cuts that prevent debris from becoming entangled within the rotating cutter. The rotating cutter shall thread onto the end of the pump shaft and be secured by a 300 series stainless steel washer in conjunction with a 300 series stainless steel flat head cap screw threaded into the end of the shaft. Both stationary and rotating cutters shall be made of 440C stainless steel, hardened to Rockwell 57-60C and ground close to tolerance. The grinder shall be capable of grinding normal domestic sewage into a fine slurry.

The impeller shall be constructed of ASTM A536-80 ductile iron and be designed for rough duty service. It shall be a ten-vane, semi-open design with four wash out vanes on the rear shroud. The impeller shall be a non-overloading design

2.3 ELECTRIC MOTOR

The stator, rotor and bearings shall be mounted in a sealed submersible type housing. The stator windings shall have Class F insulation (155°C or 311°F) and a dielectric oil-filled motor, NEMA B design (three- phase), NEMA L design (single-phase). Because air-filled motors do not dissipate heat as efficiently as oil-filled motors, they shall not be acceptable. The pump and motor shall be specifically designed so that they may be operated partially dry or completely submerged in the liquid being pumped. The pump shall not require cooling water jackets.

Supplemental cooling shall not be acceptable.

Protection against excessive temperature for single phase motors shall be provided by a heat sensor thermostat attached to the stator windings and connected in series with the contactor coil in the control panel. The heat sensor shall stop the motor if the motor winding temperature reaches 221 degrees F. The high temperature shutoff will cause the pump to cease operation, should a control failure cause the pump to run in a dry wet well. The thermostat shall reset automatically when the motor cools to a safe operating temperature. Contractor shall confirm supply voltage available prior to release for production.

2.4 MECHANICAL SEAL

Motors shall be equipped with double mechanical shaft seals to prevent leakage between the motor and pump. The seal assemblies shall consist of two Type 21 oil-lubricated rotary shaft seals in an oil-filled chamber. The materials of construction shall be carbon for the rotating faces and ceramic for the stationary faces, lapped and polished to a tolerance of one light band, with 300 stainless steel hardware, with all elastomer parts of Buna-N.

The pump shall be equipped with a seal leak detection probe and warning system.

This shall be designed to alert maintenance personnel of lower seal failure without having to take the unit out of service for inspection or requiring access for checking seal chamber oil level consistency.

There shall be an electric probe or seal failure sensor installed in the seal chamber between the two tandem mechanical seals. If the lower seal fails, contaminants which enter the seal chamber shall be detected by the sensor and send a signal to operate the specified warning device.

2.5 POWER/CONTROL CORDS

Power cord shall be SOOW water resistant 600V, UL and/or CSA approved. The single cord shall incorporate both power and sensor leads and shall be a minimum of five 12 gauge conductors. The pump shall be protected with compression fitting and epoxy potted area at the power cord entry to the pump. A separation between the junction box area of the pump and the motor, by a stator lead sealing gland or terminal board, shall not be acceptable. The power cable entry into the cord cap assembly shall first be made with a compression fitting. Each individual lead shall be stripped down to bare wire, at staggered intervals, and each strand shall be individually separated. This area of the cord cap shall then be filled with an epoxy compound potting which will prevent water contamination to gain entry even in the event of wicking or capillary attraction. The power cord leads shall be connected to the motor leads with extra heavy connectors having copper inserts with a crimped wire-to-wire connection rather than a terminal board that allows for possible leaks. The cord cap assembly shall be sealed with a Nitrile O-ring on a beveled edge to assure proper sealing.

2.6 CABLE ENTRY SYSTEM

The cable entry system shall consist of (3) separate seals. A rubber grommet that seals both outer cable jackets shall be clamped onto the cords by an end holding cap.

An O-ring shall seal the end holding cap to the bottom half of the cord cap. Both cables shall have individual conductors stripped and potted into the motor end cap with an epoxy potting compound. Potting compound shall prevent wicking of water into the motor in the event that the outer cable jacket is damaged. Cords shall be able to withstand a pull of 300 pounds to meet U.L. requirements.

PUMP STATIONS

PART 3 - BASIN ASSEMBLY

3.0 BASIN

The basin shall be constructed of filament wound fiberglass/resin. Basin capacities, dimensions and minimum burial depth to insure pipe cover shall be as shown on plans. Basin shall be capable of withstanding 150% of the anticipated maximum pressure exerted by saturated soil (120 lb/cf) at maximum bury depth. All station components shall function normally when exposed to these loadings.

The basins are filament wound and manufactured with premium E-type continuous glass fibers maintained in high constant tension during the manufacturing process.

The tension fibers squeeze out excess resin producing superior strength basins with 65% glass content.

An anti-flotation collar extending a minimum 3” beyond the O.D. of the basin wall shall be provided on all basins.

BASIN DIMENSIONS SHALL BE 48” diameter X 96” deep. Refer to plan page details for specific components and sizes.

3.1 BASIN COVER

Aluminum basin covers with hatch opening shall be provided with each basin assembly. Covers for 48” basin assemblies shall be one-piece solid w/ hinged access opening. The access opening shall have a minimum of two hinges and a lock hasp.

Covers shall be constructed of non-skid, tread-plate aluminum with a minimum thickness of ¼”. Covers shall be bolted to the basin with stainless steel cap screws.

Zinc plated nuts shall be embedded in the upper flange of the fiberglass basin for corrosion resistance and to prevent turning.

3.2 RAIL ASSEMBLY

The lift-out rail system assembly shall permit easy removal and installation of the pump and lower check valve without the necessity of personnel entering the wet well. Structural guide brackets with guide yokes of sufficient bearing strength to prevent binding shall fasten to the pump. The yokes shall mate over guide rails of a minimum of 1-inch schedule 40 pipe running between an upper rail support and the discharge case. A lower discharge nozzle, downstream from the check valve, shall be guided into a chamfered cavity in the discharge case. A shoulder on the nozzle shall bottom on the discharge case to insure alignment for a leak-tight seal. The O-rings shall affect a hydraulic seal around the nozzle when it is in its operating position. A brace, easily removable from the top of the wet well, shall be provided to lock the parts together and to prevent line surges from breaking the seal and allowing leakage. The discharge case shall have a discharge opening with piping to a discharge coupling through the basin wall.

3.3 CHECK VALVE

The lift-out check valve shall be of the ball type with a corrosion resistant neoprene ball. The ball shall be the only moving part and shall move automatically out of the path of flow, thus providing an unobstructed smooth flow through the valve body.

Upon pump shut-off, the ball shall automatically roll to the closed position to provide a positive seal against back pressure or back flow. A stainless steel check valve insert is required with the SRA-125-CV only.

3.4 LIFTOUT CHAIN

An adequate length of stainless steel lifting chain shall be supplied for removing the pump. The chain shall be of sufficient length and strength to effectively support the weight of the pump assembly during removal or installation.

3.5 DISCHARGE PIPE

Schedule 80 PVC discharge piping shall connect to the stationary discharge base lift assembly and terminate at a 1-1/2” discharge flange mounted on the basin at the height shown in the plans. The discharge flange shall have a 1-1/2” PVC solvent weld socket type hub (36” basins) or 1-1/2” NPT hub (48” basins) for attaching external discharge piping.

3.6 SHUTOFF VALVE

A PVC true union ball type shut off valve with Teflon seats or Brass gate valve shall be furnished as an integral part of the internal pipe assembly. If the discharge depth is more than 1.5 feet from the surface a stainless steel extension handle shall be supplied.

3.7 INLET FITTING

A one-piece inlet fitting for 6” and 4” SDR 40 plastic pipe shall be shipped loose for field installation as required by the installation.

3.8 JUNCTION BOX – if applicable

The junction box shall be constructed of structural plastic for corrosion resistance and of adequate thickness to provide stability and mechanical strength. The junction box shall have a fully gasketed cover that is held in place by four (4) captive stainless-steel screws with heads of adequate size so that they may easily be installed and removed without the use of special tools. The heads of the screws shall be totally encapsulated so that no metal parts are exposed. The cover shall be fastened to the main body of the junction box by means of a totally corrosion-resistant tether to prevent dropping the cover during service.

An adequate number of sealing-type cord grips shall be supplied for incoming pump and level control cords. The cord grips shall be made of non-corrosive material, such as PVC or nylon, and shall make an effective seal around the wire jacket. The cord grips shall seal to the junction box with an O-ring or gasket.

The junction box shall have a PVC solvent weld type conduit hub of adequate size to accommodate the number of wires required for pump and level control operation.

The incoming wires shall be sealed by an external EY type seal-off (supplied by others) so that condensation from the conduit or groundwater will not enter the enclosure. The interior of the enclosure shall be of adequate size to accommodate the wires and connections for pump and level control operation.

The wires running between the control panel and the junction box shall be color-coded and fastened to the pump and level controls by means of adequately sized and insulated twist lock or crimp connectors.

The junction box shall be designed to NEMA 4 standards.

3.9 LEVEL CONTROLS

Pump on, off and alarm levels shall be controlled by four (4) mercury tube float switches. Switches shall consist of a mercury tube switch sealed in a corrosion-resistant polypropylene housing with a minimum of 18 gauge, 2-wire, SJOW/A jacketed cable. The cable shall be of sufficient length to reach the junction box with no splices. The level controls shall be suspended from a stainless-steel bracket so that adjustment or replacement may be done without the use of any tools. Level controls shall be UL/CSA listed.

PUMP STATIONS

PART 4 - CONTROL PANEL

4.0 CONTROL PANEL

A NEMA 4X Stainless Steel control panel shall be furnished with each pumping unit to be installed, as shown on the plans.

The control panel enclosure shall meet the following:

1. The material to be 16-gauge Type 304 stainless steel.

2. Seams to be continuously welded and ground smooth.

3. The enclosure shall come with mounting feet to allow for wall mounting.

4. Entry shall be via a quarter-turn latch.

5. A hasp shall be installed to allow for the ability to padlock the enclosure.

The enclosure shall have a separate dead-front inner door. The inner door shall be a minimum of .080” aluminum and shall be hinged. All lights, switches, and overload resets shall be mounted through the inner door. Circuit breakers must also be mounted through the inner door.

The back panel shall be a minimum of .080” aluminum and held in place by four (4) #10 screws, which will mate to the four (4) threaded standoffs, which are molded into the enclosure.

The panel shall include pump circuit breakers, control circuit breaker (breakers rated at 10,000 A.I.C.), alarm circuit fuse, control circuit fuse, I.E.C. rated motor starters with 1-pole ambient compensated bimetal overload relays, pump hand-off-auto switches (momentary in the hand position), alarm test switch, pump run lights, seal leak lights, duplex float controller (solid state) DFC-4F, terminal blocks, ground lug and all necessary wiring and brackets.

The control panel shall be fitted with a red Lexan (polycarbonate) LED alarm light.

The light shall be approximately 3” high by 3-1/2” diameter. The globe shall be mounted on top of the enclosure with a neoprene gasket. The lens cannot be removed from the exterior of the enclosure. The lens may be removed by entering the interior of the enclosure.

The alarm shall have a bright glow and flash during high water conditions. The alarm light will go out when the water level drops.

All internal wiring shall be neat and color coded. Each wire shall be a different color or stripe (except for ground), and all incoming wires shall terminate into a box clamp type terminal block (except incoming power). All wires shall be 14GA. Type TEW rated for 105 degrees C.

A schematic diagram (showing wire color) shall be permanently fastened to the inside of the enclosure. An installation and service manual shall also be included with each control panel.

The Inner door shall include pump H-O-A switches, Pump RUN lights (green), Pump FAIL lights (red), Pump SEAL LEAK (amber).

An alarm acknowledge circuit (alarm light with buzzer) shall be provided to indicate an alarm condition. The buzzer shall be energized by either the alarm float switch or the alarm test switch A-O-T selector switch and operate in conjunction with the alarm light. The buzzer must be weatherproof and be rated for 85 DB at 10 feet.

There shall be an exterior acknowledge switch that will silence the buzzer but allow the light to remain flashing during an alarm condition.

The control panel shall be U.L. listed as an assembly.

PART 5 – ABANDONMENT OF EXISTING SEWAGE LIFT STATION

5.0 ABANDON IN PLACE THE EXISTING SEWAGE LIFT STATION

After installation and connection of the new duplex grinder station, you must pump out all liquids or waste if necessary by a licensed septic hauler.

All utilities must be disconnected and any pumps, parts, or piping must be removed.

Seal all incoming and outgoing sewer lines and force mains using watertight caps, plugs, or grout. Once all parts are removed, the bottom of the existing structure must be broken or holes drilled or punched through so that no liquid can be held in the structure.

Then demolish the structure by breaking, crushing, or completely removing the top structure/concrete slab of the wet well down to a minimum of 36 inches (3 feet) below the final restored grade. Punch holes in the bottom of the wet well to prevent it from filling up with groundwater and creating an unstable underground buoyancy issue. Crush or break the bottom/sides so the structure cannot trap water.

Fill the remaining void or excavation with clean earthen fill material. The fill must be adequately compacted to prevent future ground settling. The top layer must be finished with clean topsoil, seeded, and mulched to prevent erosion and blend into the natural area of the golf course.

Contractor must take pictures of this process.

Revised 6/8/2012

ADDENDUM ACKNOWLEDGEMENT FORM

SOLICITATION NO.:_____________

Instructions: Please acknowledge receipt of all addenda issued with this solicitation by completing this addendum acknowledgment form. Check the box next to each addendum received and sign below.

Failure to acknowledge addenda may result in bid disqualification.

Acknowledgment: I hereby acknowledge receipt of the following addenda and have made the necessary revisions to my proposal, plans and/or specification, etc.

Addendum Numbers Received:

(Check the box next to each addendum received)

[ ] Addendum No. 1 [ ] Addendum No. 6

[ ] Addendum No. 2 [ ] Addendum No. 7

[ ] Addendum No. 3 [ ] Addendum No. 8

[ ] Addendum No. 4 [ ] Addendum No. 9

[ ] Addendum No. 5 [ ] Addendum No. 10

I understand that failure to confirm the receipt of addenda may be cause for rejection of this bid. I further understand that any verbal representation made or assumed to be made during any oral discussion held between Vendor’s representatives and any state personnel is not binding. Only the information issued in writing and added to the specifications by an official addendum is binding.

Company

Authorized Signature

Date

NOTE: This addendum acknowledgement should be submitted with the bid to expedite document processing.

1. To extend bid due date to 10/13/2026 @ 1:30pm.

2. To include pre-bid sign-in sheets.

3. To publish vendor Q&A and clarifications.

Text4: CRFQ DNR27*03