We vent our tanks to the outside through a long 2" braided hose with a hosebarb connection to the bottom of the tank, after an initial rinse under pressure.
This flip open hatch on our roll-up door ("engineering control") lets us do that without letting in too many bugs and not much cold, rain and snow.
-- Alex Kopf
Lead Brewer
N[orthwoods Brewing Company
Original Message:
Sent: 10/31/2023 3:40:00 PM
From: Jason Weihbrecht
Subject: RE: CO2 monitor alarm levels - Safety
Thanks for the responses. We do have several industrial fans positioned through the facility to keep air moving with a few installed in the exterior wall to keep steady air flowing. We have additional air movers available to help move CO2 in any problem areas when an alarm does go off. We're really doing as much as we can to keep fresh air moving through the facility. I think the next logical step is to look at engineering fixes to vent tanks directly outside and things like that.
I uploaded the specific information that is posted in the MBAA safety section that lists low level alarm at 15000 and high level alarm at 30000. Perhaps that information should be changed if it's not accurate. I'd like to follow what is accepted as best practices and was curious what levels others are using for their monitoring systems.
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Jason Weihbrecht
GM of Brewery Operations
Oskar Blues Brewery
Brevard NC
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Original Message:
Sent: 10-31-2023 13:44
From: Matt Stinchfield
Subject: CO2 monitor alarm levels - Safety
Hi Jason,
Congratulations on having a CO2 monitoring system.
May I offer a different perspective? You state you are interested in increasing the alarm set-point to reduce the frequency of alarms, when you might rather be concerned with reducing the excessive levels of CO2 that are setting off alarms.
Alarm set-points below the permissible exposure limit (PEL) give the employer a chance to act before employees are exposed above legal limits. An example is an alarm set-point of 20% of the explosive concentration of methane in air. You need to rectify the atmosphere or evacuate immediately to avoid being blown up, assuming the methane continues to accumulate.
Alarm set points above the PEL are often used when the results of overexposure aren't as catastrophic as blowing up the workplace. With CO2, the thinking is that a worker could go over the all day average PEL of 5000 ppm for short periods, as long as the 8-hr time-weighted average (TWA), remains below 5000 ppm. But when an alarm sounds above 15000 or 30000 ppm, 1) what is the real concentration in the room? (A: we don't know unless we look at the display), 2) will this result in exceeding the 8-hr average? (A: we don't know unless we have integrated every measurement taken across those 8 hours), and 3) do I need to evacuate? (A: probably, if you're over 30000pm). Somewhere around 40000 ppm a worker may become impaired fast enough to interfere with self-evacuation. This value is called the IDLH (immediately detrimental to life or health). A trick for remembering IDLH is "I don't like it here!" Even so, all human bodies perform differently under exposure scenarios, so I prefer to be suspicious of the real protection afforded by the PEL or the IDLH.
Back to my original point, the primary good thing about an alarm going is off is it is telling you your process containment and exposure controls are inadequate. Don't fight the alarm, use it as a process control. An example: if the pressure gauge on a BBT rated for 15 psi was showing 40 psi, do you ask how to put more pressure into it or do you take immediate action to reduce pressure?
CO2 controls can be whatever means you invent to keep the CO2 levels in check, as long as they don't make the problem worse for others. Some examples I've seen include:
- large shop fans (sometimes automated with CO2 monitoring systems)
- opening up your more enclosed spaces during FV blowdown or turnover to promote dilution, could be as simple as opening windows or a dock door
- hard piping CO2 exhaust to a safe outside area
- implementing CO2 capture system
- substituting nitrogen where feasible
- optimizing CO2 levels in filling and lidding, and so on.
OSHA does not say CO2 has to be managed a certain way. It says workers cannot be exposed above a workday average. To win the game, do what it takes to identify sources of fugitive CO2 and manage its release to avoid overexposure.
Cheers!
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Matt Stinchfield
Author "Brewery Safety: Principles, Processes and People"
BA Safety Subcommittee
Safety Coach
Guilford, VT
802-258-8748
Original Message:
Sent: 10-30-2023 14:06
From: Jason Weihbrecht
Subject: CO2 monitor alarm levels - Safety
We've been using a multi sensor CO2 monitoring system in our facility. We currently have them set up to have a blinking strobe light go off when a sensor reads over 5000 ppm. It doesn't take much to set off a sensor depending on what process is going on since they are installed near the ground. I'm concerned that if the strobe lights are constantly blinking they will start to be ignored. Does anyone have any guidance on what levels these monitors should be set to alarm? I found a resource on MBAA that had low level alarm set at 1.5% (15000 ppm) and high level alarm at 3.0% (30000 ppm). The source was listed as CO2meter.com (maybe not the most reliable source). The only trustworthy guidance I can find is that the OSHA allowable limit is 5000 ppm average over the course of an 8 hour shift. I'm interested in increasing the limits so that they are only going off when there is a real concern, but want to make sure it's backed by sound science with safety in mind. I'm curious what others are doing in their facilities.
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Jason Weihbrecht
GM of Brewery Operations
Oskar Blues Brewery
Brevard NC
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