This is an excellent set of detailed specifications and vendor reports! To make an informed decision, we need to compare each vendor’s offering against your detailed requirements (the “Table 1” sections) for each valve tag.

Let’s break down the analysis by vendor and then provide a consolidated recommendation.


Overall Assessment

After reviewing all three vendor quotes against your detailed specifications, it’s clear that none of the vendors have provided a perfect quote that aligns 100% with all of your stated requirements without requiring further clarification or accepting significant deviations. Each quote has its strengths and weaknesses, but also critical discrepancies.

The most common and significant discrepancies across multiple vendors are related to:

  1. Valve Sizing: Many vendors propose valve sizes (or reduced trim bodies) that differ from your specified line size, sometimes without clear initial justification in the provided documents.
  2. Trim Material/Seating (especially for Class IV and Cavitating/Flashing service): Ambiguity or direct mismatch on trim material for the specified leakage class and for critical cavitating/flashing services.
  3. Fail Position (FC/FO): Some quotes contradict the required fail position.
  4. Material of Construction: Some minor discrepancies in body material grades.

Vendor-Specific Analysis

1. Baker Hughes (Masoneilan Valves)

Strengths:

Weaknesses / Discrepancies:

2. Samson Quote

Strengths:

Weaknesses / Critical Discrepancies:

3. CTi Controltech (Valtek Mark One / Kammer)

Strengths:

Weaknesses / Critical Discrepancies (Primary Quotes):


Recommendation

Given the current state of the quotes:

  1. Eliminate CTi Controltech (Primary Offer): Their primary quotes are largely mismatched in size, type, and fail position. Accepting this quote would require re-engineering most of your valve specifications. The “alternative” rotary valves are not a direct like-for-like replacement for globe valves unless previously discussed. This quote, as is, is the weakest.

  2. Proceed with Caution and Clarification for Samson: While Samson’s quote provides reasoning for its sizing deviations, the extent of these deviations (e.g., quoting a 6" valve for a 2" line) is very significant. You must confirm with your engineering team if these size changes are acceptable given the process conditions, physical space, and potential system impacts. Crucially, the ambiguous or potentially mismatched trim material for cavitating/flashing service (131-TV-0371) is a critical safety and reliability issue that must be resolved with concrete confirmation of hardened stellite or equivalent. If these two points can be resolved satisfactorily, Samson could be a contender, but it requires significant work and acceptance of large deviations.

  3. Strongest Candidate: Baker Hughes (Masoneilan Valves)

    Why Baker Hughes is the preferred choice (with caveats):

Immediate Actions Recommended:

1. For Baker Hughes (Masoneilan):
* Request Clarification on Sizing: Send them a list of all valves where their “Valve Body Size” differs from your “Pipe Size and Rating” and ask for detailed engineering justification (Cv calculation, pressure drop, velocity, noise, etc.) for each proposed body size reduction. Confirm these smaller bodies can be physically installed.
* Confirm Trim Materials: Specifically clarify the meaning of any asterisks or generic descriptions for trim/retainer materials to ensure they meet the “Stainless Steel plug, seat, and trim; Cavitating service to have hardened stellite plug, seat, and trim” requirement. Pay special attention to 131-TV-0371.
* Confirm Material (131-LV-0369): Confirm if the 316L SS for the body is acceptable instead of Carbon Steel.

2. For Samson (as a backup/comparison):
* Request Resolution of Critical Trim Issues: Demand explicit confirmation (with specific material codes and type) that the trim for 131-TV-0371 (flashing service) is hardened stellite and suitable for the application. Resolve the “PTFE/METALLIC” ambiguity for all valves.
* Re-confirm Sizing Deviations: If your engineering team can’t accept their current sizing, request a re-quote for the original specified sizes, acknowledging their previous noise/choked flow explanations, and see if they can meet the requirements at the specified sizes with different trim options or technologies.
* Address Travel Exceedances: Ask for re-sizing or different trim options to bring maximum travel within the <80% limit.

3. For CTi Controltech:
* Unless you are open to significant design changes and rotary valves, it’s advisable to communicate that their primary quote does not meet the specified requirements for size, type, or fail position on multiple items, and request a comprehensive re-quote that strictly adheres to the provided data sheets.

By prioritizing Baker Hughes and focusing on resolving their specific, manageable discrepancies, you will likely arrive at the most compliant and reliable solution based on the information provided.