Bioprocessing and botanical extraction sit at opposite temperatures and use the same sanitary exchanger families. A mammalian cell bioreactor is held at 37 C and a microbial fermenter at 30 to 37 C, in both cases within a tenth of a degree, by a temperature control unit that circulates water through the vessel jacket and through a small exchanger that adds plant steam heat or chilled water cooling on demand. Media is sterilized at 121 C for 15 to 30 minutes in batch or continuously through a heater, hold and cooler, and harvest and buffers are chilled to 2 to 8 C for downstream steps.
Extraction plants for CBD, hemp and other botanicals chill ethanol to -40 F (-40 C) before it meets the biomass so that waxes and chlorophyll stay behind, recover the ethanol by evaporation and condensation, and winterize the crude by chilling it in ethanol to drop the remaining lipids. Hydrocarbon plants condense propane and butane after the extraction vessel. The exchangers are sanitary plate or tube-in-tube on propylene glycol or a low-temperature fluid, with condensers on the solvent vapor.
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A 20,000 liter microbial fermenter can throw several hundred kilowatts; the cooler is sized on that peak at the warmest chilled water with 30 percent margin. At the cold end, glycol at -45°F is about 60 cP, so ethanol chillers are sized on the glycol side.
Bioreactor exchangers are small and precise; extraction exchangers are cold and sized on solvent rate. Both are chosen by the fluid and the separation needed.
| DUTY / CONDITION | RECOMMENDED CONSTRUCTION | WHY |
| Bioreactor TCU heater and cooler on jacket water | U-Tube | Compact steam-to-water and chilled-water-to-water sets with free expansion through daily cycling; no product contact so single tubesheet is acceptable |
| Continuous media sterilizer, 121 C heater, hold and cooler | Double Tubesheet | WFI-based media against plant steam and cooling water; the gap protects the batch |
| Harvest, buffer and product chilling to 2 to 8 C | Double-Wall Plate | Small volumes, tight approach on chilled glycol, leak visibility between plates; opens for inspection |
| Ethanol chilling to -40 F for extraction | Gasketed Plate | Highest coefficient on a thin solvent; gaskets rated for ethanol and -40 F; low holdup of cold solvent |
| Crude oil in ethanol winterization, viscous at -20 to -40 F | Single Tube-in-Tube | Large bore for a fluid that thickens as it chills; lipids that drop out do not plug a plate channel |
| Ethanol or hydrocarbon vapor recovery after evaporation | Vapor Condenser | Sanitary shell-and-tube condenser sized on evaporator vapor rate; sub-cooled return to the solvent tank |
A bioreactor temperature control unit is a small closed water loop with a pump, a heater and a cooler. The heater is a steam-to-water exchanger, often a U-tube or a plate, that adds heat during start-up and trims during the run; the cooler removes the metabolic heat of a dense culture, which on a 2,000 liter mammalian reactor is a few kilowatts and on a 20,000 liter microbial fermenter can be several hundred. The exchangers are sized on the peak cooling load at the warmest chilled water with a 30 percent margin, and the heater on the start-up time from ambient. Turndown is the design problem: the same cooler that removes 300 kW at peak must remove 3 kW at the end of the run without cycling the jacket temperature, which is done with a small approach, a well-sized control valve and a loop volume that damps the swings.
Continuous media sterilization heats media to 121 C, holds it for a validated time in a sloped hold tube and cools it to inoculation temperature, and it is the process that decides whether the batch is contaminated. The heater is double tubesheet because the media is made on WFI and the utility is plant steam; the cooler is double tubesheet for the same reason on tower water; regeneration is media-against-media through a third double tubesheet unit where the plant wants the steam savings. Media with dissolved sugars and salts fouls the heater over a campaign, and the run length is set by area margin the way a dairy UHT heater's is.
Ethanol chilling to -40 F is a viscosity and gasket problem. Ethanol at -40 F is about 4 cP, glycol at -45 F is about 60 cP, and the coefficient on the glycol side collapses; the exchanger is sized on the glycol side, the glycol flow is generous, and a low-temperature fluid replaces propylene glycol where the chiller can supply it. The plate gaskets are chosen for ethanol at that temperature, and the frame is insulated and vapor-sealed so the plates do not ice from room air. The holdup of a plate pack is small, which matters when a cold solvent is also a flammable one.
Solvent recovery is a condenser sized on the evaporator's vapor rate at the chilled water or glycol available. Ethanol at 173 F atmospheric boiling condenses on tower water; under vacuum at 100 to 120 F it needs chilled water, and the condensate is sub-cooled before it returns to the tank so the vent does not carry ethanol. Hydrocarbon recovery condenses propane and butane at pressure on chilled glycol, and the exchanger, the skid and the electricals are specified for a classified area.
Anything that touches media, harvest or product is 316L electropolished to 15 to 20 Ra, drainable and CIP and SIP compatible. TCU exchangers on jacket water are utility equipment and do not need that finish, which is why a plant can put a plain U-tube on the jacket loop and save the pharmaceutical specification for the sterilizer and the buffer cooler. HeatX quotes both grades on one order.
Single-use bioreactors move the temperature control to the jacket of the bag holder, and the TCU exchanger is the same small water-loop heater and cooler. Pilot and clinical suites often want one skid that serves several vessels; that is a larger TCU with a distribution header, sized on the coincident peak.
Winterization dissolves crude extract in ethanol and chills it to -20 to -40 F for 24 to 48 hours so that fats and waxes precipitate before filtration. The chiller is a tube-in-tube or wide-gap plate because the solution thickens and drops solids as it cools. Decarboxylation heats the extract to 220 to 250 F for an hour; that is a jacketed vessel with a hot oil or steam set behind it, and the fume condenser is a small vapor condenser on tower water.
For bioreactors: vessel size, peak cooling load or organism and cell density, setpoint and tolerence, chilled water and steam available. For extraction: solvent, flow, inlet and outlet temperatures, chiller fluid and temperature, evaporator vapor rate for condensers, and the area classification.
Call and talk it through with an engineer: 1-805-484-2992
At the vessel wall. Anything that can touch media, harvest, buffer or product is specified to the pharmaceutical standard; the TCU heater and cooler behind the jacket are utility equipment and are bought that way. The practical form of that line is two line items on the user requirement specification: a jacket loop pair in 304 or 316 with material reports and a hydrotest certificate, and the sterilizer, regenerator and chillers with the full turnover package.
Proof that the fastest-moving element of media saw 121 C for the validated time. The hold tube is sized on the fastest particle, not the mean velocity: in laminar flow the centerline moves twice as fast as the average, so a hold tube that gives 15 minutes on paper gives 7.5 at the center. The qualification run uses the maximum pump output, an RTD at the hold tube outlet driving a divert valve, and a hold tube sloped upward with no pockets. The heater earns its place by carrying enough area that the outlet still reaches 121 C at the end of a fouled campaign, not only on day one.
It is unless the sterile side is kept at the higher pressure. Raw and sterile media share one tube wall in the regenerator, and a pinhole leaks toward the lower pressure. The sterile side already carries back pressure above the 15 psig at which 121 C media would flash, so the raw side is throttled to stay below it and a differential pressure alarm proves it. The saving is real: 10 gpm of media heated from 20 to 121 C is about 900,000 Btu/h, and a regenerator recovering 70 percent cuts the steam heater to roughly 270,000 Btu/h. Both the regenerator and the pressure arrangement go on the P&ID together; a double tubesheet alone does not protect against a tube that leaks inward.
To food or dietary supplement GMP, which asks for materials and pressure records rather than finish readings. A hemp or botanical extractor typically works under 21 CFR 111 or 117, so the package is material reports for the 316L product side, a food-contact statement for every gasket, the hydrotest record and the ASME data report where the shell is stamped. The reviewers who do read the drawings are the fire authority and the insurer, and they want the design pressure of anything holding cold solvent and the area classification of the skid.
Yes, but not one that touches the culture. The bag sits in a jacketed holder, and the holder is served by the same small water loop heater and cooler that a stainless vessel uses; at 2,000 liters of mammalian culture that is a few kilowatts, about 10,000 Btu/h for 3 kW. Upstream the media is still made on WFI and chilled or sterilized through stainless, and downstream the harvest still goes through a chiller to 2 to 8 C before capture. A single-use suite ends up with fewer validated exchangers than a stainless one, not none, and the ones it keeps are product contact.
Loop heaters, loop coolers, still condensers and sanitization heaters for water that must stay as it was made.
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Cool the draw, not the loop: 80 C to 25 C at the valve, then drain dry and steam.
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WFI and purified water, point-of-use cooling, bioreactor loops and extraction chilling, built to ASME BPE.
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