Glass Lined Equipment Repair and Maintenance

Summary

This manual contains information and procedures on the maintenance and repair of glass-lined equipment. Glass-lined equipment is susceptible to failure in the field from poor operational practices or mishandling during maintenance activities. Failures may be reduced and avoided by establishing good practices and training personnel in them. This publication identifies reasons for failure, the difficulties and limitations of field repair, goals for improving the state-of-the-art, and a course of action to improve the reliability and longevity of repairs. It is a unique compilation of information that includes lots of useful input from MTI member companies and manufacturers.

The major manufacturers of glass-lined equipment offer field repair and reglassing to pro-long the life of equipment. Repair services are also provided by skilled contractors. Plants can also perform various types of repairs, depending on the skill and experience of the personnel involved.

Glass-lined steel and glass-lined stainless steel possess the following attributes:
  • Corrosion resistance. Glass has the widest range of corrosion resistance of any material of construction. Most processes are developed in the laboratory in glassware. If the laboratory equipment shows no sign of corrosion or etching, it is likely that glass-lined equipment will be resistant. Glass resists corrosion in most acid solutions, except for hydrofluoric acid. It resists corrosion in alkali solutions at moderate temperatures.
  • Cleanliness. Glass does not contaminate products, and protects their color and purity.
  • Smoothness. Glass linings minimize friction, reducing demands on agitation equipment. Glass also resists viscous or sticky product buildup.
  • Superior vacuum service. Although glass linings are comparable in pressure and temperature ratings to other types of premium lined equipment, the tight bond between glass and steel imparts superior vacuum performance.

The design and fabrication of glass-lined equipment is substantially different from corrosion resistant alloys. Designs and fabrication practices cannot be transferred from alloy to glass. Some of the differences are as follows:

Nozzles

  • Alloy nozzles are welded to the top head and may have reinforcing pads. Glass-lined steel nozzles are first swaged to create a protrusion from the vessel head to which nozzles are welded with split lap ring backup flanges. Larger diameter glass-lined steel nozzles such as manways and dome covers use a J-clamp or J-bolt closure design instead of conventional bolting. The J-bolt closure design is used to minimize the bending moment created in the larger diameter flanges, versus a conventional ANSI or DIN bolted flange. Nozzle reinforcing pads are not permitted because they create glassing difficulties. 
  • Threaded couplings can be welded to alloy vessels for pressure gauges, inert gas addition, and other such uses. They are not permitted with glass-lined vessels because they cannot be glassed. All nozzles must be flanged. 
  • Alloy vessels may have any size nozzle. Glass-lined steel nozzle size is based on the steel thickness and the distance between the nozzles. The fabricator can advise the minimum allowable nozzle size, but 1-½ in. diameter is the minimum in certain applications.
  • Nozzle lengths are limited in glass-lined steel, to minimize the amount of thermal movement or distortion that can occur, due to the required high temperature firings.
  • Nozzle loadings are limited in glass-lined steel to avoid damaging the lining. As a rule of thumb, maximum nozzle load is typically set at 100 pounds per inch of nozzle diameter (for example, 400 pounds for a 4-inch nozzle). Most glass-lined equipment manufacturers have published tables of allowable nozzle forces and moments. Expansion joints are useful in decoupling piping loads from vessel nozzles. However, expansion joints create a weak link (or an additional failure mode) in the piping system and should be scrutinized very carefully from a process hazards analysis standpoint. In higher pressure systems, expansion joints can also create unacceptably high thrust loads if not properly constrained. Generally speaking, for systems that operate above ambient temperature, a piping designer should evaluate the piping layout and ensure that nozzle allowable loads are not exceeded.

Internals

  • Alloy vessels are normally supplied with four baffles bolted or welded to the vessel wall. Glass-lined steel vessels are normally supplied with one or two baffles, depending on vessel size. Each baffle must be installed through a nozzle, reducing the number of nozzles available for other purposes. There is a relatively new design with built-in baffles.
  • Internal coils can be supplied in alloy vessels, but not in glass-lined steel.

Jackets

  • Alloy vessels have jackets with built-in baffles to introduce turbulence. Glass-lined steel vessels use jacket agitation nozzles located in the bottom head and shell of the jacket. This creates turbulence and high flow rate in the jacket to counteract the lower thermal conductivity of the glass.
  • Glass-lined steel vessels are equipped with a diaphragm in the bottom head of the jacket to compensate for expansion and contraction of the jacket, which limits thermal stress to the lining.

Pressure/Temperature Rating

  • The upper temperature limit of standard glass-lined steel is 500º F (260º C); specially formulated glass for high-temperature applications can withstand 650º F (345º C). The lower temperature limit is -94º F (-70º C). Any temperature below the minimum requires the base metal to be changed to stainless steel.
  • The maximum pressure rating for glass-lined steel is determined by the vessel size. Normal pressure rating is 100 to 150 psi, but higher pressure ratings are available on special order.
  • The glassed shell of a standard glass-lined steel vessel already contains a built-in corrosion allowance. The shell is relatively thick (above design allowable thickness) to maintain dimensional stability during multiple firings). The steel jacket is usually fabricated with a 1/16 -in. corrosion allowance.

Gaskets

  • PTFE envelope gaskets are the most commonly used and recommended gaskets for glass-lined steel. It is important to note that a wide range of designs and quality of envelope gaskets are available and not all are equal. Therefore, the user should consider issues like maximum operating temperature, presence of permeants, consequences of failure, and expected service life when selecting a gasket manufacturer and envelope gasket design. Additionally, for smaller nozzles (12-in. diameter and lower), monolithic expanded PTFE gaskets have been used successfully. The advantage of a monolithic gasket is largely related to greater permeation resistance and better conformability, along with elimination of some failure modes that envelope gaskets experience. See Appendix C, Bolting and Gasketing, for guidance on flange makeup and gasket selection.

Externals

  • Gear boxes with motors are flange-mounted on alloy vessels. In glass-lined steel vessels they must be mounted on a series of bosses located on the top head or main cover. Likewise, mechanical seals for glass-lined steel agitators are more specialized and in many cases more expensive and larger in diameter than their metallic mixer counterparts.

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Table of Contents

Introduction…..15

1.1 Overview

1.2 History of Glass-Lined Steel

1.3 Pfaudler Reactor Systems

1.4 DeDietrich Process Systems

1.5 Tycon, SpA

1.6 Applications of Glass-Lined Equipment

1.7 Available Types of Glass-Lined Equipment

1.8 Differences Between Alloy and Glass-Lined Equipment Designs

 

Working Inside Glass-Lined Equipment……23

2.1 Clothing and Shoes

2.2 Tools

2.3 Lighting

2.4 Air Movers

2.5 Mats

2.6 Ladders and Platforms

2.7 Respect for Manways

2.8 Bringing Accessories Into a Glass-Lined Vessel

2.9 Installing a One-Piece Agitator

2.10 Installing Glass-Lined Removable Blade Agitators

2.11 Installing Flange-Mounted Baffles, Dip Tubes, and Spargers

2.12 Installing Holder-Mounted Baffles, Dip Tubes, and Spargers

 

Failure Modes and Effects in Glass-Lined Equipment……31

3.1 Internal Impact

3.2 External Impact

3.3 Hydroblasting

3.4 Abrasion

3.5 Cavitation

3.6 Crushing

3.7 Bending

3.8 Vibration

3.9 General Thermal Shock

3.10 Local Thermal Shock

3.11 Welding Near Glass

3.12 Restricted Flexibility from Large Fillet Welds

3.13 Expansion of Steel

3.14 Electrostatic Discharge

3.15 Spark Testing

3.16 Minimum Available Glass Thickness

3.17 Corrosion by Water

3.18 Corrosion by Acids

3.19 Corrosion by Alkalis

3.20 Corrosion by Salts

3.21 Degradation of Tantalum Patches and Plugs

3.22 Attack of Furan Cements

3.23 Attack of Silicate Cements

3.24 Damage to PTFE Components

3.25 Corrosion from External Spills or Wet Insulation

3.26 Damage from Chemical Cleaning of Jacket

3.27 Flange Face Spalling

 

In-Service Inspection of Glass-Lined Equipment……67

4.1 Inspection Frequency

4.2 Internal Inspection

4.3 External Inspection of Shell and Jacket

4.4 Inspection Inside Jacket

4.5 Inspection of Lifting Lugs and Supports

4.6 Glass Thickness Measurement

4.7 Jacket Thickness

4.8 Spark Testing

4.9 DC Spark Testing

4.10 AC Spark Testing

4.11 Generic Spark-Testing Procedure

4.12 Inspection of Plugs and Patches

4.13 Remote Visual Inspection and Photography

4.14 Mechanical Seal and Agitator Drive Inspection

4.15 StatiFlux Testing

 

Repair of Glass-Lined Equipment…..79

5.1 Repair Preparation

5.2 Repair Materials

5.3 Tantalum

5.4 Other Metals

5.5 Furan Cement

5.6 Sodium Silicate Cement

5.7 Potassium Silicate Cement

5.8 Epoxy Putty

5.9 PTFE

5.10 Repair Methods

5.11 One-Piece Plug

5.12 Three-Piece Plug

5.13 Patch

5.14 Inside Metal Sleeve

5.15 Outside Metal Sleeve

5.16 Inside-outside Metal Sleeve

5.17 Outside PTFE Sleeve (PTFE Insert Sleeve)

5.18 Inside-outside PTFE Lined Sleeve

5.19 Smear-on Putty

5.20 Metal Repair

5.21 Gold Inlay for Flange Face Restoration

5.22 Thermal Spray Coating

5.23 Repair Training

 

Polishing……129

6.1 When to Polish

6.2 Polishing as Part of the Repair Process

6.3 Light (Surface, or Rough) Polishing

6.4 Full (Luster) Polishing

6.5 Polishing Tools and Supplies

6.6 Polishing to Repair Nozzle (or Clamp Flange), Outside Edge Chips,

or Spalls

6.7 Polishing to Repair Nozzle (or Clamp Flange) Gasket Faces with

Mechanical Impacts or Pinholes

6.8 Polishing to Repair Nozzle (or Clamp Flange) Gasket Area with Scratches

6.9 Polishing to Repair Mechanical Impact Damage

6.10 Polishing to Repair Spalls

6.11 Polishing to Repair Mechanical Damage, Chips, and Micro-impacts

6.12 Light Polishing Procedure

6.13 Full Polishing Procedure

 

Reglassing……143

7.1 Determining Need to Repair or Reglass

7.2 Development of Reglass and Vessel Preparation Requirements

7.3 Preparation for Reglassing by Vendor

7.4 Glass Application

7.5 Glass Lining Defects (DIN 28063)

7.6 Other Glass Lining Defects

7.7 Dimensional Tolerances

7.8 Problems During Firing

7.9 Glass Specifications

7.10 Vendor Selection