Sanitary Heat Exchanger Installation & Service

Surface area driven by duty and approach temperature, whether double-wall or double-tubesheet construction is required, material and specified surface finish, gasket and elastomer selection, and then the installed scope: tie-in piping, supports, insulation, instrumentation, controls integration, post-installation passivation, documentation and qualification. The largest single surprise is utility generation, since an exchanger needing clean steam or chilled capacity that does not already exist adds a generation scope, which Paul builds alongside the exchanger.

When a failure of the barrier between the utility side and the product side would allow utility fluid to reach product. A single-wall unit carrying plant steam or untreated cooling water against product is a contamination path if the wall is breached, and the leak may not be immediately detectable. Double-tubesheet and double-wall designs provide a detectable interstitial space, and where a leak could reach product the utility itself may need to be clean steam or compendial water regardless of how the jacket is labelled on the drawing.

Fouling, on either side. A product-side film or utility-side scale insulates the surface and degrades heat transfer gradually. Cleaning restores duty, but the more useful question is why it fouled: usually velocity too low to keep the surface swept, or wall temperature high enough to bake product onto it. Differential pressure trending will show fouling developing before the approach temperature does.

Treat it as a contamination event rather than a maintenance item. A cracked plate, failed gasket or tube leak breaches the barrier between utility fluid and product, and the pressure differential only determines which direction the contamination travelled. Take the unit out of service and integrity-test before returning it. Where a leak could put utility fluid into product, the utility itself should be clean steam or compendial water, and a double-tubesheet or double-wall design should have been specified.

Plate heat exchangers dominate food and beverage because they give very high heat transfer in a small footprint, can be opened for inspection, and their capacity can be changed by adding or removing plates. Gasketed plate units suit most duties; where product viscosity or particulates are high, a scraped-surface or tubular unit is the better answer because plates blind. Tubular exchangers handle particulates and are easier to clean in place, at the cost of size. Triple-tube designs provide double separation between product and service fluid, which matters where cross-contamination would be serious. The controlling selection questions are particulate size, viscosity, fouling tendency and whether the unit must be openable for inspection.

Four types cover almost everything. Gasketed plate exchangers, the default for low-viscosity liquids, offering high efficiency and expandable capacity but with gaskets as a maintenance item and a leak path. Tubular and shell-and-tube designs, tolerant of particulates and pressure, easier to clean in place, larger for the same duty. Triple-tube designs, which put a service fluid on both sides of the product tube with a vented interstitial space so any leak is detected before fluids mix. And scraped-surface exchangers for viscous, sticky or crystallizing products where a rotating blade continuously clears the wall. Selection follows the product rather than the duty: viscosity and particulate size decide the type before heat load does.

Pharmaceutical selection is driven by cleanability and by what happens if the two fluids meet. Ask first whether a leak between service and product fluid is tolerable; where it is not, a double tube sheet or triple-tube arrangement with a monitored interstitial space is appropriate rather than a gasketed plate unit. Confirm the product side can be cleaned in place with demonstrated coverage and drains fully, because a unit that holds a heel cannot be validated. Specify surface finish to ASME BPE on product contact. Confirm materials, since 316L is standard but chloride-bearing service may need more. And confirm it can be sterilized if the process requires it, with condensate able to drain from every part.

316L is the default for product contact and is adequate for compendial water, most buffers and most product streams. The decision points that push beyond it are chlorides and temperature. Chloride-bearing solutions at elevated temperature will pit 316L, and the step up is a higher-molybdenum grade such as AL-6XN or 904L, then nickel alloys such as Hastelloy C-22 for genuinely aggressive chemistry. Titanium is used where chlorides are severe but reducing conditions are absent, commonly on seawater or brine duty. On the service side, materials can often be less expensive since only the product side needs hygienic specification. Gasket material matters as much as metal: EPDM for general and steam duty, PTFE-faced where solvents or oils are present.

Plate units transfer heat far more efficiently per unit volume, so they are smaller and cheaper for the same duty, they can be opened for inspection and cleaning, and capacity is changed by adding plates. Their weaknesses are gaskets, which are a maintenance item and a potential leak path between fluids, intolerance of particulates which blind the narrow channels, and limited pressure and temperature range. Shell and tube units are larger and less efficient but handle particulates and viscous fluids, take higher pressures and temperatures, clean in place more readily, and with a double tube sheet give positive separation between fluids. For compendial water cooling after distillation, shell and tube with double tube sheet is the conventional choice for exactly that reason.

Start with the serial or National Board number on the drawings or the turnover file, then request the manufacturer’s data report. Registered units can be traced through the National Board. Paul Industries can then measure, inspect and document the unit so a re-rating or replacement rests on verified data.

When the process fluid would attack stainless or nickel alloys and the pressure and temperature sit inside the plastic’s limits. Hot acid baths, plating lines and high-chloride streams are typical. The larger surface area it needs has to be weighed against the cost of the alloy it replaces.

Paul Industries selects, installs and ties in shell and tube, plate, tube-in-tube and double-tubesheet heat exchangers for process plants. Units are set and oriented for drainability, access and CIP or SIP, then connected to product, steam, hot water, chilled water or glycol lines, with orbital-welded sanitary piping to ASME BPE on the process side. Weld, material and pressure-test records come with turnover.