Correct, the distance between end walls is 47 ft.
If I understand this correctly, you're saying the dominant (constraining) load is along the height of the backfill, not the width of the wall, right? I'm curious why the IRC would stipulate buttress every 50 feet?
As noted in any earlier comment, my structural engineer made it clear that the floor diaphragm, which is set inside and anchored to the basement wall, is a key part of getting the 6" wall to pass. Even without that detail, I wouldn't dream of backfilling without the floor system in place.
BTW...
@Dik, Section A on your attachment answers my question about positioning double perimeter rebar. Thx. The 21" distance I mentioned is to top of wall (beginning of above-grade framing). I think those hook prescriptions are where there's a nearby adjacent surface that's perpendicular to the opening.
@NS4U, I'm overseeing the project myself. The only impact will be during backfill. I'm guessing the bobcat can position 90% of the dirt without violating the 5 ft restriction. I'll have a couple of extra men on hand to assist with bringing backfill up to final grade adjacent to the house.
@dik wrote: > At openings I run horizontal and vertical wall steel past the opening by 2'
@jayrod wrote: > My own spec for openings in residential walls is just additional straight rebar on all sides that extends a minimum distance past the opening.
My design already has the extra full height...
Wow, I appreciate all the replies!
There were a couple of logistical reasons that would have been much more consequential than concrete cost that drove my desire to go with 6" if at all possible. The engineer's first pass at 6" thickness had two #4 rebar matts, which he agreed would be...
I'm in the process of building the basement for my own new home. As an engineer myself, I understand each engineer develops their own prescriptive or 'template' designs for certain common details. In that context, there's a detail in my structural engineer's wall rebar design for which I'd like...
@11241, my original post questions this assumption. But your point, which echoes what SPDL310's wrote, properly recognizes that friction (due to roughness) doesn't contribute much to overall valve resistance. I'm satisfied that the velocity exponent for a valve is probably close to 2.
Thanks for your reply. I didn't mention in my op but I also regressed the fan coil pressure drop curves based the manufacturer's modeling tool. I checked several models & sizes and the exponent comes out to 1.88 +/- 0.01. For similar reasons that you posit for valves, we can expect fan coils to...
I created a spreadsheet to calculate hydronic loop pressure drops. To make the spreadsheet more functional, I regressed several AquaPex friction tables for the velocity range of interest. AquaPex tables are unusual in that they account for water temperature, providing a higher degree of accuracy...
The tank lid will have 4" XPS and high reflectance/low emissivity coating on top. Upper 4 feet of tank body (corrugated culvert) will have three layers of flexible EPS wrap (~R-18), middle 4 feet will have two layers and the bottom portion one layer, with 1" XPS under the slab. I'm not sure yet...
These chillers are little 2-ton monoblocks with an integrated variable speed pump (the WiLo I referenced in my previous comment) and a Mitsubishi inverter compressor. The chiller's control board uses PWM to maintain the user-selected LWT and Hx delta-T. The chiller's internal control board...
See concept drawing. This is for an off-grid home near Phoenix. To take maximum advantage of TES capacity, the load side flow rate will vary from less than 1 gpm with single zone call for smallest zone and water is in low 40's, up to about 13 gpm when water temperature climbs into low 60's...
Ziggy wrote "don't forget the system curve"
Well, that's why I asked the question... I need to know the PD's at every point in the loop to develop the system curve, no?
Since my original post, I found a very helpful resource for this exact scenario: Caleffi Idtronics #17 Thermal Storage in...
LittleInch wrote: "as your pumps are pd type then flow can be assured regardless of pressure loss"
But I need to know what the losses are at various conditions in order to select my pumps. Depending on what's happening at the Tee, the worst case may be when both pumps are operating. The system...
