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I’d go with a robokit and pressurise the system, never seen it cause the pipework to fail, and if it stays open vent the air in the system will cause bigger problems in time.
 
Normally no inserts used
Seen that happen Shaun quite a few times bud i had the same issue with the Worcester classic system I posted on here couple of months a go pipework was poorly installed cast your mind back I sealed it but as I said the working pressure was set to a bar not much more than a open vent system worcesters dont work on a pressure switch so you can run it on low system head low as 0.5 bar worth considering bud good luck kop

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Excellent!

An old boy told me the pump will last longer if it is running on the cooler return water, hence the old way of doing it with the pump on the return. Don't bleed the rads with the pump running, though ;)

Nos da

I do a lot of plumbing repair jobs, and you are correct about pumps lasting on the return much longer. I noticed over the years that pumps on oil boilers fitted to the return where lasting 20 or more years and their rubber washers weren’t perishing.
 
Nice rads kop
 
ive decided to put the pump on the return and keep the feed and vent to spec if it does pump over will give him the option to leave or seal it
That wasn't one of your original options, but that would be OK.
Should then be open vent - cold feed - pump - boiler. You definitely don't want the cold feed on the discharge side of the pump or there's a good chance there will be negative pressure somewhere, if pump DP is 8m.
As I'm sure you know, the open vent and cold feed should be no more than 150mm apart to avoid risk of over-pumping, but where they are in the circuit relative to other kit is irrelevant.
 
Virtually all open vent systems (except gravity to cylinder) I know of in my area are done with the vent off the flow at cylinder and feed off the cyl return.
I would guess they are old systems. I bought 1st house in 1972 which was piped like that, but it was going out of favour vs boiler - open vent - cold feed - pump then or shortly after, due to the issue of seesawing causing aerated water entry. I modified it, and piping was simpler as the cold feed point was then directly below the F/E tank.
 
That wasn't one of your original options, but that would be OK.
Should then be open vent - cold feed - pump - boiler. You definitely don't want the cold feed on the discharge side of the pump or there's a good chance there will be negative pressure somewhere, if pump DP is 8m.
As I'm sure you know, the open vent and cold feed should be no more than 150mm apart to avoid risk of over-pumping, but where they are in the circuit relative to other kit is irrelevant.

No it wasn't as it would be under neg pressure

Can't get the vent and feed before pump unless it's on the return as it's an ab roof, which isn't the best as it won't vent if the boiler boils

It's a bloody catch 22
 
as it would be under neg pressure
Not sure I understand that. It won't be under negative pressure if the cold feed is on the pump suction pipe.
Can't get the vent and feed before pump unless it's on the return as it's an ab roof, which isn't the best as it won't vent if the boiler boils
Hard to say without knowing the details. You've clearly looked at lots of options so it's unlikely I can add anything, but I'm game to try if you want, no doubt others here will too.
The bit about the boiler boiling - is it solid fuel? I didn't think boiling was an issue with gas or oil, as there are control and limit-stats.
 
Not sure I understand that. It won't be under negative pressure if the cold feed is on the pump suction pipe.

Hard to say without knowing the details. You've clearly looked at lots of options so it's unlikely I can add anything, but I'm game to try if you want, no doubt others here will too.
The bit about the boiler boiling - is it solid fuel? I didn't think boiling was an issue with gas or oil, as there are control and limit-stats.

it would go

pump on return pushing into boiler
feed on flow
vent on flow

there is an always risk in certain circumstances eg if a stat goes bad etc
 
pump on return pushing into boiler
feed on flow
vent on flow
I'd be a bit nervous with that arrangement. I did sketch below based on some assumptions:-
Pump DP 8m, total system loss 8, 3m across boiler, 5m across rads and pipework
TWL in F/E tank 3m above fill point on pipe
Boiler, pump and rads are all at same level
Shows pressure -2m after the rads. The assumptions won't be spot on and it could be refined to allow for different levels, so it might be OK in practice, specially if it's a tall building so plenty of head from the F/E tank. On the other hand, it might be worse.
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there is an always risk in certain circumstances eg if a stat goes bad etc
What precautions are normally taken which you can't do on this job? I'm curious because it might apply to my house!

PS I hope you're charging the customer double time!
 
tbh these days seal the system unless its ropy like the one im doing

and some boilers have flow switches in dont fire unless theres flow
 
Why not seal without pressurising. Use the header as top up, with gate and non return fitted. Sealed system controls as required with heat only or system boiler ( Worcester Cdi used to not need minimum pressure to operate, but check with them).
 
Why not seal without pressurising. Use the header as top up, with gate and non return fitted. Sealed system controls as required with heat only or system boiler ( Worcester Cdi used to not need minimum pressure to operate, but check with them).

thats not a bad shout would the non return open tho also would need a prv
 
Non return is to stop the water backing up into the header. Therefore system controls required, i.e PRV and expansion vessel required either external or internal to boiler (system). Doesn’t need filling loop as header acts as top up vessel. Works a treat without stressing existing pipe work. As the system is sealed and there is no open vent non return will stay shut as for air to get in water would need to get out.
 
Non return is to stop the water backing up into the header. Therefore system controls required, i.e PRV and expansion vessel required either external or internal to boiler (system). Doesn’t need filling loop as header acts as top up vessel. Works a treat without stressing existing pipe work.

yea but would it open under gravity and not stick
 
Have got two systems like this operational now in their sixth year and no problems.

head of the tanks vs the position of check?
 
Top of system for header. Followed by gate or lever in downfeed, so you can turn system of and for easy replacement of check valve. I positioned them in airing cupboard. Check valve can be anywhere between isolation valve and where it tees into the system.
 
Top of system for header. Followed by gate or lever in downfeed, so you can turn system of and for easy replacement of check valve. I positioned them in airing cupboard. Check valve can be anywhere between isolation valve and where it tees into the system.

Trying to work out how much head you have
 
Use the header as top up, with gate and non return fitted.
Does the gate valve stay open in normal operation?

I can't see how this differs from just having an expansion vessel, but with pre-charge pressure somewhat lower than normal.
Still need to put the expansion vessel connection in the right place, to avoid having negative pressure somewhere.
 
I am actually having the same problem trying to decide how I convert a gravity hot water/pumped rads to all pumped on a very old system, without pump over or corrosion.
I converted mine about 20 years back. Old cast iron floorstanding boiler, gravity HW, pump next to boiler, pumping downwards. No controls. Cold feed to boiler return.
Scrapped the boiler and installed wall-mounted condensing. Moved the pump to the airing cupboard, added diverter valve (system W), open vent, cold feed and DV in the airing cupboard. Added cylinder and room stats. Re-used the gravity 28mm pipes as pump suction and cylinder return.
Still working OK.
 
Does the gate valve stay open in normal operation?

I can't see how this differs from just having an expansion vessel, but with pre-charge pressure somewhat lower than normal.
Still need to put the expansion vessel connection in the right place, to avoid having negative pressure somewhere.
Gate valve stays open. Ans yes you can just seal, add vessel and PRV and have virtually no pressure. Its just convenient using the existing header instead of a filling loop if its already there.
 
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