Hans-Georg Baunach

ISH 2011

Dear Ladies and Gentlemen,

The experience of recent years has taught us that the demand for efficient and renewable heating technology has gone up and down with the price of oil. A look at the price trend shows us how the market psyche works: the rising price is only really recognised when the previous peak is exceeded. Although the oil price has more than doubled since the beginning of 2009, this has hardly been discussed in public.

Only now, when the oil price has exceeded the three-digit mark of 100 $ and the political unrest in North Africa is fuelling expectations of further price rises, is the issue returning to the agenda with a vengeance.

It is good for those who can offer their customers a solution to an acute problem, because now "efficient" and "regenerative" heating will once again be of interest outside of political Sunday speeches.

We will show you how to combine solar energy, heat pumps, biomass and combined heat and power generation into an effective system - customised, brand-independent and reliable.

See our efficient hydraulic solutions for yourself at the next ISH from 15 to 19 March 2011 in Frankfurt am Main! You will find us in hall 9.0 on stand F64. Our team is looking forward to your visit.

Yours, Hans-Goerg Baunach

Hydraulics seminar

The efficiency of heating systems, whether with condensing boiler technology or regenerative heating technology, is becoming increasingly important for customers, and not just because of rising energy prices. But how can you guarantee your customers this efficiency?

We would like to invite you to the hydraulics seminar on this topic on Friday, 1 April 2011 from 9.45 to 15.00. The event will take place at Rheinstraße 7, 41836 Hückelhoven, in GSZH, House 5, Media Room.

Professional tip: Pump speed and flow temperature

More efficiency at the buffer tank with less effort

Some regenerative heat generators, such as wood or pellet boilers or CHP units, may only be operated with a fixed return temperature. For this purpose, a return flow increase (RLA) is used, which feeds parts of the heat generator flow into its return flow. Very often, the pump speed is selected unnecessarily high, which reduces the efficiency of the buffer storage loading.

Flow temperature decisive

The amount of heat that can ultimately be absorbed by the buffer storage tank depends not least on the flow temperature: if, for example, a 1 m³ buffer storage tank is heated from 30°C to 75°C, it can absorb up to 52.5 kWh; at 90°C flow temperature it would be 70 kWh - a whopping plus of 33%! A boiler with 35 kW would therefore have a maximum running time of 2 h at 90°C flow temperature, but only 1.5 h at 75°C.

Heat quantity = 7/6 × buffer volume × delta-T
Heat quantity = 7/6 × 1 m³ × (75-30)K = 52.5 kWh
Heat quantity = 7/6 × 1 m³ × (90-30)K = 70.0 kWh

Volume flow decisive

How can the flow temperature of a heat generator with RLA be raised? Quite simply by reducing the volume flow! If a heat generator with 35 kW output has a flow rate of 1 m³/h, its flow temperature is 30 K higher than the return temperature; with 2 m³/h it is only 15 K higher. If the fixed return temperature is 60°C, a flow rate of 2 m³/h results in a flow temperature of 75°C, and 1 m³/h results in a flow temperature of 90°C. Furthermore, halving the volume flow saves 7/8 or 87.5% of the electrically expended pump power.

Delta-T = 6/7 × power : flow rate
Delta-T = 6/7 × 35 kW : 1 m³/h = 30 K
Delta-T = 6/7 × 35 kW : 2 m³/h = 15 K

In the end, it's the layering that counts

But that's not all: in order for the buffer to be able to absorb the entire amount of heat, the 30°C cold water it contains must not be mixed with hot water from the heat generator. This is because loading can only be carried out until the buffer has reached 60°C at the bottom. After that, the return temperature can no longer be regulated to 60°C; the heat generator must be switched off. Responsible for the mixing of hot and cold water in the buffer tank is the volume flow through the buffer tank: the greater it is, the greater the turbulence and mixing of hot and cold water. It is therefore worth taking a look at the volume flows.

Figure 1a

Figure 1a shows a buffer tank less than half full, which is loaded by a boiler with 35 kW of heat. Water comes out of the lower buffer connection at a temperature of 30°C. The return lift (RLA), which keeps the boiler return temperature at 60°C, is flowed through by the pump with a volume flow of 1 m³/h. The delta-T is therefore 30. The delta-T is therefore 30 K and the flow temperature 90°C. The RLA therefore mixes water at 30°C and 90°C in equal parts of 0.5 m³/h each into the return. Consequently, the water flow rate through the buffer tank is also 0.5 m³/h.

Figure 1b

In Fig. 1b, on the other hand, the pump of the RLA was set to twice the volume flow of 2 m³/h. The delta-T at the heat generator is thus 15 K and the flow temperature 75°C. Thus, the delta-T at the heat generator is 15 K and the flow temperature is 75°C. Now two parts 75°C (1.33 m³/h) have to be mixed with one part 30°C (0.67 m³/h) to get the desired 60°C in the return. So the water flow through the buffer tank is now 0.67 m³/h, also a plus of 33%. Only this plus is a big minus for stratification! Because 33% more water throughput also means 33% more flow velocity, which results in 78% more kinetic energy, because: If you go 33% faster, you have a 78% longer braking distance.

Figure 2a

Figure 2a shows the buffer tank more than half full. The return flow increase (RLA) keeps the boiler return temperature at 60°C; it is flowed through by the pump with a volume flow of 1 m³/h. The delta-T is therefore still 30 K and the flow temperature 90°C. The pump is not used for this purpose. The delta-T is therefore still 30 K and the flow temperature 90°C. The 35 kW boiler now takes the water from the lower buffer connection at a temperature of 45°C. The RLA therefore now mixes two water flows. The RLA therefore now mixes two parts of water at 45°C (0.67 m³/h) with one part at 90°C (0.33 m³/h) in the return. Consequently, the water flow rate of the buffer tank is now 0.67 m³/h.

Figure 2b

In Fig. 2b, the pump of the RLA was again set to double the volume flow of 2 m³/h. The delta-T is thus 15 K and the flow temperature is 75°C. Thus the delta-T is 15 K and the flow temperature 75°C. Now 75°C must be mixed with 45°C in equal parts (1.0 m³/h each) to obtain the desired 60°C in the return. The water flow through the buffer tank is therefore now 1.0 m³/h, which corresponds to a plus of 50%. However, if you drive 50% faster, you have a braking distance that is 125% longer.

Everything at a glance

The summary is absolutely clear:

Everything speaks for the smallest possible volume flow through the heat generator. This raises the question: How small can the volume flow actually be? Not so small that the maximum permissible flow temperature of the heat generator is exceeded! So it should be as small as possible, but as large as necessary. The best way to try this out is to bring the heat generator up to maximum output and then adjust the pump speed so that the highest possible flow temperature is reached, which ensures trouble-free operation.