When youre installing a propane tank, some of the first questions that come up are about logistics. Deciding what size and type of propane tank you need and understanding requirements about where propane tanks need to be placed are fundamental first steps each of which depends on a lot of data points and complex regulations. It can be easy to get into the weeds.
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So, we thought wed untangle some of the complexity for you. AmeriGas walks through these questions in more detail when you receive your personal quote, but to help you start looking ahead, weve created this rundown of the most common sizes of residential propane tanks and the basics of where to place them. (Itll also help you visualize what, say, 1,000 gallons of propane looks like.)
Propane tanks for home heating and appliances fall into three basic categories: above-ground tanks, underground tanks, and vertical propane tanks. Above-ground and underground propane tanks are designed to hold large amounts of propane required to power your home, and vertical tanks are lower capacity, typically used for one or two appliances. Here are the basics of each:
Available in sizes that hold 125 gallons to more than 2,000 gallons of propane
Horizontal profile, placed on your property, typically in an out-of-the-way location (more on that below)
Used for everyday propane heating, cooling, appliances
Available in most of the same sizes as above-ground tanks, ranging from 250 gallons to 2,000 gallons or more
Larger underground tanks can be placed closer to the house and property lines, so underground propane tanks may be a good option if you expect high usage but dont have a lot of yard space to work with
Underground tanks are buried just under the ground; the depth depends on the tank size usually one or two feet deeper than the tanks height
Used for everyday propane heating, cooling appliances, etc.
Smaller tanks, typically less than 125-gallon size
Stand vertically, usually alongside the home
Used to fuel a limited number of appliances, such as water heaters or fireplaces
After youve decided on a size and type, its time to figure out where the propane tank will be located on your property. As a homeowner, your priority may be maintaining curb appeal or maximizing yard space. At the same time, your goals will need to also allow easy access to the tank and, importantly, comply with safety regulations. On the upside, most of these needs are compatible, enabling us to find a spot for your propane tank that is both inconspicuous and safety compliant.
The very first thing we check off the where can we place the propane tank list is the safety code. Propane tanks are installed following regulations established by the National Fire Protection Association specifically NFPA 58, the code that addresses all aspects of propane safety. And of all the NFPA 58 rules, the one with the greatest impact on residential propane tank installation deals with propane tank placement. The NFPA established minimum distances to reduce the risk of fire in the relatively rare case of a propane tank leak. These tank location standards also keep propane exhaust from escaping into building interiors. All AmeriGas installments follow these regulations and AmeriGas services only tanks that are located according to the NFPA code.
The requirements about propane tank placement are essentially driven by two questions: How close to the driveway can a propane tank get to allow safe and easy access for refilling? In the rare case of a leak or other problem, how far away does the tank need to be to keep people safe?
For answers, the key numbers to keep in mind are 10 and 25. For 125- to 500-gallon propane tanks, the distance is at least 10 feet from any building and from any property line. Same with underground propane tanks that hold up to 2,000 gallons: The minimum distance, from either a building or a property line, is 10 feet. For above-ground tanks of 1,000 to 2,000 gallons, the safe distance increases. These must be placed at least 25 feet from a building or property line.
In addition to following the 10- and 25-feet rules, all propane tanks that receive refill deliveries must be at least 5 feet from your driveway.
Smaller propane tanks are treated a little differently because they typically stay closer to the home. Tanks smaller than 125-gallon size must be placed at least 10 feet from windows or air conditioners, and they must be placed at least 5 feet from any crawl-space openings.
Check out the table [DIRECTION] for a quick reference on propane tank location requirements by size. (Reminder: Some tank placement requirements may vary by state, so check your local regulations for up-to-date information.)
Table: Propane tank placement from key spots
The size of the propane tank you choose will depend on your planned usage; well work with you to determine the optimal option. As for type, you have more flexibility. Above-ground tanks are made to withstand all weather conditions, and the placement requirements make it unlikely that the tank will interfere with the regular, everyday use of your yard. Underground tanks stay out of view and may seem like they would leave more room for other backyard items. However, the area above underground tanks should remain clear of everything but landscaping. So the decision is mostly a matter of your personal taste.
Time to pick a propane tank? Click here to get your quote online now
Related Content:
Propane Tank Installation: A Live Blog
Safety Series: Propane Leak Checks
The Pros and Cons of Tank Ownership
How to Hide Your Propane Tank
Propane Tanks Go to blog list page filtered for the category
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LPG tank design - Pressure/temperature
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(Mechanical)
(OP)
29 Nov 22 14:33Dear Eng-tippers,
Am on an LPG bottling unit project and we are struggling to determine the design pressure for our LPG storage tanks. Seeking on your help on that matter.
Client specifications gives the following.
Maximum operating pressure 11.5 bar @50°C
Operating teperature min/max 10/+60°C
Operating pressure Ambient temperature min/max : -1.4/47.6°C
Ambient temperature for design min/max : -5/+55°C
Black body temperature : 85°C
the Engineering department considered the design pressure actually as the vapour pressure of the LPG at 60°C. The question here is if the black body temperature impacts only the mechanical design (selection of material allowable stress) or should it be considered also for design pressure determination (which will be the vapour pressure of the LPG at 85°C).
Replies continue below
(Petroleum)
29 Nov 22 15:06This BB temperature keeps going up! Last time I seriously looked it was 70C.The issue is always this - does the heating of 50% of the thing - vessel, pipe, cylinder etc - really mean that the entire content get to that temperature.I've always argued that this really only impacts an empty or very nearly empty pipe or tank, so I suppose from your view you need to see if that happens.Or build a sun shade.And also you need to define "LPG". This can be anything from 100% Propane to 100% butane.... Makes a HUGE difference to the Pressure /temp relationshipYou might need some good relief systems, but then as the LPG vaporises it reduces in temperature so it all gets a bit complex.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
(Chemical)
29 Nov 22 15:26Quote (API , "Design and Construction of LPG Installations" says)
4.2 DESIGN PRESSURE AND TEMPERATURE
4.2.1 The design pressure of LPG vessels shall not be less
than the vapor pressure of the stored product at the maximum
product design temperature. The additional pressure resulting
from the partial pressure of noncondensable gases in the vapor
space and the hydrostatic head of the product at maximum fill
shall be considered. Ordinarily, the latter considerations and
the performance specifications of the relief valve require a differential between design pressure and maximum product
vapor pressure that is adequate to allow blow down of the pressure relief valve (see API RP 520).
I hope this helps! Also, contact an experienced LPG tank fabricator, or three, and see what is their past practice.Good Luck,Latexman
(Petroleum)
29 Nov 22 15:33Also you don't quote min design temp.For LPG that could go as low as -42C if it's pure propane. Now sure that's at very low pressure, but there could be a lot of contraction.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
(Mechanical)
(OP)
29 Nov 22 15:53Thanks LittleInch,Latexman, agree with you that LPG composition makes difference, our gas composition is 70% butane 30% propane, but uselss here to go into calculation details, I want to make clear the design parameters.
Also I confirm that solar effect calculations make things much more complex (although we did it for scénarios where tank is full, half full and empty), I suppose that should a kind of assumption/rule in regard to considering operating temperature Vs Black body temperature for tank design.
(Mechanical)
29 Nov 22 17:43Here in the USA LPG tanks are sold as mass commodity items, they are typically called "bullet tanks" and are designed to ASME VIII and NFPA-58The selection of design/BB/min/max temperatures and design pressures is done within NFPA-58---Standard operating pressure and temperature: 250 PSI @ 125° F---Standard materials SA612, SA516-70This might also help ...Where will your tank be located, Ali ?What is your governing code of construction ?MJCroninSr. Process Engineer
(Petroleum)
29 Nov 22 17:56Typically these bullets are covered with earth or I've seen other smaller surface mounted tanks provided with a large sunshade to stop this issue from occurring.A sunshade is a lot cheaper than designing your system for 85 C....
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
(Chemical)
29 Nov 22 23:08This max op pressure of 11.5barg at 50degC seems low for LPG, but maybe this is because your C3 content is much lower than regular commercial LPG - okay.
You should also specify LDT - lower design temp with a view to avoid low temp brittle fracture, which should be auto refrigeration temp of this LPG grade. Any Chary impact testing must be done at the plate manufacturer and provided with material certification. Also confirm you wont be storing LPG in this storage vessel with C3 any higher than 30%, else LDT will be lower. Even at the current min operating temp of -10degC, which would required an LDT of -15 to -20degC, Charpy impact testing of low temp carbon steel plate would be a must.
With Tunisia being on the edge of the Sahara, agreed black body temp would be high, but 85degC seems excessive. I've not seen blackbody temp higher than 70degC for your region. Ask to see blackbody temp calcs; take note infra red radiation (which enables heating) is typically 50% in terms of intensity of total solar radiation. Also note blackbody temp derivation takes no credit for natural convection for vessels typically sitting out in the open.
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