Control Valves

Chapter 16 - Installation

The purpose of this chapter is to describe the following topics for the benefit of the professionals assigned the responsibility of installing a control valve: planning the installation, the receipt-inspection of the valve at the job site, the installation of the valve in the piping, preoperational tests, and specifics involving popular valve types.

In 1993 a recommendation was made to the ISA Standards and Practices Board to form a committee to prepare a standard that would address specifications for the receipt, storage, installation, and calibration of instruments and control systems, including control valves. Such a standard had not been issued as of the time of this writing. The Manufacturers Standardization Society has issued a Valve User Guide that addresses some of the shipping, storage, and installation concerns discussed in this chapter [Ref. 1], Most manufacturers will supply instructions for receipt, inspection, storage, and installation as well as start-up, servicing, testing, and the like.

Planning

DRAWINGS

An instrument installation specification can be prepared by plant personnel or by an engineering contractor. It will be useful whether the installation is to be done by plant personnel or by an outside contractor (see Reference 2).

The reader is referred to Reference 3 for a detailed discussion of the project documentation that is usually needed. All documents in their latest revisions should be available at the job site. Often, up-to-date documents are available from a master computer that can be accessed at job site terminals. Flow loops needing control valves are typically delineated on process flow diagrams, which show fluid flow rates along with piping, pumps, heat exchangers, vessels, and other related mechanical and electrical equipment. These diagrams may also show temperatures, pressures, and compositions in start-up, normal, minimum, maximum, emergency, and shutdown conditions.

Another related drawing is a piping (or process) and instrumentation drawing (P&ID), which will show all pieces of major equipment, including control valves and the instruments in the control loops. Tag numbers of all devices appear on the P&ID, with the possible exception of some accessories. If positioners, limit switches, and the like do not show on the P&ID they should be shown on the instrument installation drawings. If the P&ID shows process conditions, a process flow diagram may not be needed nor have been generated.

Instrument installation drawings, location drawings, and piping isometrics, if available, give detailed information. If these drawings cannot be adhered to, typically for reasons of mechanical interference, the site engineer should consult with the design engineer for a resolution and then get the drawings revised. The drawings should have notes for any special spacing requirements. The process engineers may not be aware of spacing requirements; the control valve specifier should take any such requirements into consideration and see that the information is passed on to the other disciplines. Typical notes advise on straight pipe lengths upstream and downstream, which may be needed to assure the proper flow pattern of the fluid entering and leaving the control valve as well as minimum clearances for such servicing as removing topworks and other maintenance procedures. Such spacing is often shown in vendors' catalogs. Also, piping isometrics show reducing fittings (eccentric reducers, straight-side down, may be necessary for draining through the valve) and isolation, bypass, bleed, and drain valves. If the piping downstream of a control valve can be shut off, a pressure relief valve is usually installed to protect against overpressure, which can be caused by a rise in temperature of a trapped liquid or by leakage through the "closed" control valve.

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