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Chapter 4 - Water-to-water heat pump

Chapter 4 - Water-to-water heat pump

4 water / water heat pumps

4.1 Groundwater as a heat source

If the appropriate boundary conditions exist, the thermal energy generation via the groundwater can represent a very efficient form of thermal use of the subsoil for heating and / or cooling purposes. When planning, building and operating well systems for thermal use of the subsoil, the water law requirements and the respective country-specific regulations must be observed. For thermal use, with a view to the efficiency of the system as well as groundwater protection, groundwater near the surface with a free groundwater level (same groundwater-bearing layer) should primarily be used.

When using deeper groundwater levels, special protective measures are required. The planning and execution of well systems must be carried out by relevant planning offices or appropriately qualified specialist companies in the well construction trade. The recommendations of guideline VDI 4640 Part 2 must be observed here. Information about the productivity of the groundwater stock and the chemical composition of the groundwater is absolutely essential. A test borehole, which can later be converted into a well, is recommended for assessment. The manufacturer's recommendations for the quality of the well water must be observed (see Section 4.2). If the water quality does not meet the manufacturer's specifications, either a heat pump model with a suitable evaporator (stainless steel heat exchanger) or an intermediate circuit with a screwed stainless steel plate heat exchanger (see Section 3.6 and Section 4.3.4) can be used. The evaporator must be protected from frost damage, for example by means of temperature monitoring or an intermediate circuit that is operated with an anti-freeze mixture. The manufacturer's specifications are to be observed. The intermediate circuit requires additional energy to operate the brine pump and reduces the heat source temperature by around 3 K, which leads to a reduced coefficient of performance.

For small systems, groundwater is a rather difficult heat source to assess if there is no experience with systems in the immediate vicinity, because the effort for a test borehole is very high. The test hole cannot be used if it is unsuitable. For large systems, the costs for a test borehole and for a pumping test are of lesser importance; greater depths (up to 50 m) are economically justifiable here. The most important criteria for a system decision and preliminary planning are summarized below:

  • Approval according to the Water Management Act (WHG) by the lower water authority

  • Distance between suction and suction wells: at least 15 m in the direction of flow of the groundwater flow

  • Recommended minimum distance between boreholes and existing buildings: 2 m

  • The stability of buildings must not be endangered.

Temperature range of the groundwater

7 ... 12 ° C

Area of application of the water / water heat pump

7 ... 25 ° C

Guide value for the amount of water required

min. 2 m3/ h for 10 kW heating capacity or
min. 220 l / h for 1 kW evaporator output

Availability

  • All year round

Possibility of use

  • monovalent

  • monoenergetic

  • bivalent (alternative, parallel, partially parallel)

  • bivalent regenerative

Development effort

  • Approval procedure (lower water authority)

  • Delivery wells / absorption wells with airtight closure of the well heads

  • Water quality (water analysis)

  • Piping system

  • Well pump

  • Earthworks / construction work

 

Maintenance instructions In order to be able to guarantee safe operation of the heat pump, it must be serviced at regular intervals. The following work can also be carried out without special training:

  • Cleaning the inside of the heat pump

  • Cleaning the primary circuit (dirt trap, particulate filter, ...)

In addition, the tightness of the heat pump and the functionality of the refrigerant circuit must be checked at regular intervals.

NOTE
Further information and country-specific standards for leak testing heat pumps can be found at www.glendimplex.de/wartungsvertraege.

NOTE Further information on the maintenance of heat pumps can be found in the installation instructions for the heat pump.

Work on refrigerant-carrying components may only be carried out by appropriately trained and instructed personnel.

4.1.1 Dimensioning information - heat source water

The heat source of the water / water heat pump must be designed for the cooling capacity of the heat pump. This can be calculated from the heating power minus the electrical input power of the heat pump in the design point. The basic rule for the heat source is that the power Q transferred to the heat pump's evaporator0 must provide. The following applies: Evaporator output Q0 (kWth) = Heating capacity QC. (kWth) - electrical power consumption of the compressor Pel (kWel)

NOTE A heat pump with a higher coefficient of performance has a lower electrical power consumption and thus a higher cooling capacity with a comparable heating output.

When replacing an old heat pump with a newer model, the output of the heat source must therefore be checked and, if necessary, adjusted to the new cooling output.
Dimensioning the well pump

The water volume flow depends on the performance of the heat pump and is conveyed by the well pump. Depending on the output, the mass flow should be selected so that at the lowest heat source temperature (7 ° C) there is a temperature spread across the evaporator of 2 - 3 Kelvin. The water throughput specified in the device information of the heat pump corresponds to a temperature spread of the heat source of approx. 3 K. In addition to the volume flow, the pressure losses in the well system and the technical data of the pump manufacturer must be taken into account. In doing so, pressure losses in pipelines, internals and heat exchangers connected in series must be added.

** The back pressure corresponds to the free compression of the well pump at the operating point minus the pressure difference between the highest point of the well system and the water level (level) in the well (manometer).
Temperature difference heat source groundwater

The Water Management Act (WHG) defines the difference between the inlet and outlet temperature of a water / water heat pump. These values are defined as follows:

  • Permissible change in temperature of the water to be introduced compared to the extraction temperature of the groundwater: +/- 6 K

  • Minimum temperature of the water to be introduced: 5 ° C

  • Maximum temperature of the water to be introduced: 20 ° C

4.1.2 Development of the heat source groundwater

From a well depth of 8 to 10 m, the groundwater heat source is suitable for monovalent heat pump operation, as this only shows slight temperature fluctuations (7-12 ° C) all year round. In principle, the approval of the responsible water authority must be available for heat extraction from groundwater. It is generally issued outside of water protection zones, but is tied to certain conditions, such as a maximum withdrawal quantity or a water analysis. The amount withdrawn depends on the heating output. For the operating point W10 / W35, Table 4.1 contains the required withdrawal quantities. The planning and construction of the well system with delivery and absorption wells should be entrusted to a drilling company certified by the international heat pump association with a seal of approval or approved according to DVGW W120. In Germany, VDI 4640 sheets 1 and 2 must be taken into account.

Heat pump

Stainless steel spiral heat exchanger

Well pump (recommended for standard)

Circulation pump with poor water quality and use of an intermediate circuit with plate heat exchanger

Pressing well pump2

Cold water throughput heat pump

Heat pump heating output

Heat pump cooling capacity

Evaporator pressure loss

Well diameter from

Motor protection

 

 

 

 

bar

m3/H

kW

kW

Pa

customs

A.

WI 10TU

x

UWE 200-95

not mandatory 1

1.55

2.2

9.6

8.0

6200

4th

1.4

WI 14TU

x

Grundfos SP 3A-3

not mandatory 1

1.4

3.1

13.3

11.1

14000

4th

1.4

WI 18TU

x

Grundfos SP 5A-3

not mandatory 1

1.5

4.0

17.1

14.2

15200

4th

1.4

WI 22TU

x

Grundfos SP 5A-3

not mandatory 1

1.2

5.3

22.3

18.5

21400

4th

1.4

WI 35TU

 

Grundfos SP 8A-3

WSI 32TU (SI 26TU with Stratos Para 30 / 1-12)

1.3

8.2

35.6

30.0

22000

4th

on site

WI 45TU

 

Grundfos SP 14A-3

WSI 45TU (SI 35TU with Magna3 40-80F)

1.7

10.0

46.2

38.0

37000

4th

on site

WI 65TU

 

Grundfos SP 14A-3

WSI 65TU (SI 50TU with Magna3 65-80F)

1.15

16.0

68.5

58.0

25,000

6th

on site

WI 95TU

 

Grundfos SP 30-2

WSI 90TU (SI 75TU with Magna3 65-100F)

1.75

23.2

99.0

82.0

55000

6th

on site

WI 120TU

 

Grundfos SP 30-2

WSI 110TU (SI 90TU with Magna3 65-100F)

1.54

27.7

118.5

98.3

21500

6th

on site

WIH 120TU

 

Grundfos SP 30-2

WSIH 110TU (SIH 90TU with Magna3 65-100F)

1.55

28.1

122.5

100.0

30800

6th

on site

WI 180TU

 

Grundfos SP 46-2

WSI 150TU (SI 130TU with Magna3 65-150F)

1.7

42.1

177.0

144.5

41500

8th

on site

1 Stainless steel spiral heat exchanger as standard! 2 Pay attention to the counter pressure of the well system in order to avoid bearing damage to the well pump!
Tab.4.1: Dimensioning table of the minimum required well pumps for water / water heat pumps for W10 / W35 for standard systems with closed wells. The final definition of the well pump must be made in consultation with the well builder.

4.2 Water quality requirements

Regardless of the legal regulations, the groundwater must not contain any settable substances and the iron (<0.20 mg / l) and manganese (<0.10 mg / l) limit values must be observed in order to prevent the heat source system from becoming clogged . Experience shows that soiling with grain sizes over 1 mm, especially with organic components, can easily lead to damage. Grainy material (fine sand) does not settle if the specified water flow rates are adhered to. The dirt trap included in the scope of delivery of the heat pump (mesh size 0.6 mm) protects the evaporator of the heat pump and must be installed directly at the inlet of the heat pump.

The use of surface water or salty waters is not permitted. Initial information about a possible use of the groundwater can be obtained from the local water supply company.

  1. Water / water heat pumps with welded stainless steel spiral heat exchanger (Tab.4.1)
    A water analysis regarding corrosion of the evaporator is not necessary if the annual mean temperature of the groundwater is below 13 ° C. In this case, only the limit values for iron and manganese have to be complied with (ocher formation). At temperatures above 13 ° C (e.g. waste heat recovery), a water analysis must be carried out in accordance with Tab.4.2 and the resistance of the stainless steel evaporator of the heat pump must be verified. If one characteristic is negative “-” or two characteristics are “0” in the “Stainless steel” column, the analysis is to be assessed as “Negative”.

  2. Water / water heat pumps with copper-brazed stainless steel plate heat exchangers Irrespective of the legal provisions, a water analysis according to Tab. 4.2 must be carried out in order to prove the resistance for the copper-soldered evaporator of the heat pump. If one characteristic is negative “-” or two characteristics are “0” in the “Copper” column, the analysis is to be assessed as “Negative”.

 

Assessment criterion

Concentration range (mg / l)

copper

Stainless steel> 13 ° C

 

Assessment criterion

Concentration range (mg / l)

copper

Stainless steel> 13 ° C

settable substances (organic)

 

0

0

 

oxygen

<2
> 2

+
0

+
+

ammonia
NH3

<2
2 to 20
> 20

+
0
-

+
+
0

 

Hydrogen sulfide (H2S)

<0.05
> 0.05

+
-

+
0

chloride

<300
> 300

+
0

+
0

 

HCO3- / SO4th2-

<1
> 1

0
+

0
+

electr. conductivity

<10 µS / cm
10 to 500 µS / cm
> 500 µS / cm

0
+
-

0
+
0

 

Hydrogen carbonate (HCO3-)

<70
70 to 300
> 300

0
+
0

+
+
0

Iron (Fe) dissolved

<0.2
> 0.2

+
0

+
0

 

Aluminum (Al) dissolved

<0.2
> 0.2

+
0

+
+

free (aggressive) carbon dioxide

<5
5 to 20
> 20

+
0
-

+
+
0

 

SULPHATES

up to 70
70 to 300
> 300

+
0
-

+
+
0

MANGAN (Mn) released

<0.1
> 0.1

+
0

+
0

 

SULPHITE (SO3), free

<1

+

+

NITRATES (NO3) solved

<100
> 100

+
0

+
+

 

Chlorine gas (Cl2)

<1
1 to 5
> 5

+
0
-

+
+
0

PH value

<7.5
7.5 to 9
> 9

0
+
0

0
+
+

 

 

 

 

 

Tab 4.2: Resistance of copper-brazed or welded stainless steel plate heat exchangers to water constituents "+" normally good resistance; "0" Corrosion problems can arise, especially if several factors are rated with 0; "-" should not be used; [<less than,> greater than]


Even if the limit values for the water quality specified in Table 4.2 are adhered to, constant deposits of iron, manganese and lime can impair the performance of the heat pump, up to and including complete failure of the well and heat pump system. Therefore, the well system must be checked regularly and, if necessary, the well pump system cleaned.

4.3 Development of the heat source

4.3.1 Direct use of water of consistently good quality

Water with temperatures between 7 ° C and 25 ° C can be used directly with a water / water heat pump if the compatibility of the groundwater, cooling water or wastewater has been proven according to Tab. 4.2. In the event of a negative assessment of the water quality or if the water quality changes, a heat pump with an intermediate circuit (see Section 4.3.2 ff) must be used.

4.3.1.1 Heat source groundwater

Extraction wells The groundwater, which the heat pump uses as a heat source, is taken from the ground via a well. The well output must ensure continuous extraction for the minimum water flow through the heat pump.
Inlet fountain The groundwater cooled by the heat pump is fed back into the ground via an injection well. This must be drilled at least 15 m behind the delivery well in the direction of the groundwater flow in order to exclude a "flow short circuit". The intake well must be able to absorb the same amount of water as the delivery well can deliver.

 

Fig. 4.1: Example of an integration of the water / water heat pump with delivery and absorption wells

 

4.3.1.2 Heat source waste heat from cooling water

Temperature range
When using water with temperatures between 8 ... 25 ° C, it must first be clarified whether the cooling water is available in sufficient quality and quantity and to what extent the heat generated by the heat pump can be used. If the compatibility of the cooling or waste water according to Table 4.2 is permanently ensured, a water / water heat pump can be used.

4.3.2 Indirect use of water as a heat source

If the compatibility of the water cannot be proven or there is a risk that the quality of the water can change, an intermediate heat exchanger must be connected upstream to protect the heat pump. The intermediate circuit increases operational reliability, especially when a brine / water heat pump is used and the secondary circuit is thus filled with brine. A water / water heat pump with an intermediate heat exchanger should only be used if the use of brine as a heat transfer medium is not permitted and permanent water temperatures above 10 ° C (e.g. waste heat from production processes) can be guaranteed.

4.3.3 Planning recommendation groundwater / intermediate circuit heat exchanger

Brine heat pump with intermediate circuit heat exchanger (WSI packages)
(Use of groundwater, closed system)
The minimum brine outlet temperature must be set to> 1 ° C. A thermostat must be provided in the heat source circuit that switches off the heat pump in the event of a fault (strap-on thermostat included in the scope of delivery of the WSI packages).
Water heat pump with intermediate circuit heat exchanger
(Groundwater use, open system)
Installation of a flow switch is recommended because there can be time delays until sufficient groundwater is pumped or the volume flow can drop abruptly during operation.
Water heat pump with stainless steel spiral heat exchanger for groundwater
(Groundwater use, open system)
A stainless steel spiral heat exchanger ("Spirec") increases the reliability of the heat pump system. The use of a flow switch (DFS) contributes to a further increase in operational safety.

4.3.4 Heat exchanger (System separator) to protect the heat pump

The external The heat exchanger must be planned according to the heat pump used, the existing temperature level and the water quality. In the simplest case, the heat exchanger consists of PE pipes that are laid directly in the heat source and therefore do not require an additional heat source pump. This cost-effective alternative can be used if the volume of the heat source is sufficiently large (e.g. waste water basin, flowing water).
Otherwise, screwed plate heat exchangers are to be used.
The heat exchanger is configured depending on the following parameters:

  • Water quality

  • Operating temperature range

  • Cooling capacity of the type of heat pump used

  • Water flow primary and secondary circuit

Depending on the software version of the heat pump control, the frost protection of a brine / water heat pump can be adjusted. If the standard value is increased from -8 ° C to +4 ° C, the heat pump is switched off at brine outlet temperatures below +4 ° C.
Assembly of the heat exchanger For optimal heat transfer, the heat exchangers must be connected using the counterflow principle. They must also be protected from contamination. For this purpose, a dirt trap with a mesh size of approx. 0.6 mm must be installed in front of the inlet of the heat exchanger. Compensators should be used to reduce the transmission of structure-borne noise and vibrations (e.g. heat source pumps ...).
Maintenance of the heat exchangers Depending on the degree of pollution in the water, the heat exchanger can become dirty, reducing its transmission capacity. Regular cleaning should take place to prevent this. For example, the so-called CIP process (cleaning-in-place) is used. The heat exchanger is rinsed on site with a weak acid such as formic, citric or acetic acid to remove deposits.

Heat pump

 

WI35TU

WI45TU

WI65TU

WI95TU

WIH120TU

WI 120TU

WI 180TU

Connection of the generating circuit

customs

1 ½ "

1 ½ "

1 ½ "

2 "

2 "

2 ½ "

2 ½ "

Heating water flow rate VHW

* m³ / h *

5.9

7.9

11.5

16.9

21.2

20.6

22.2

Pressure loss ΔpHW

Pa

10,000

17900

9200

24500

25,000

36000

36000

Generator circuit pump M16

 

Stratos Para 30 / 1-12 **

Stratos Para 30 / 1-12 **

Magna3 40-80 F.

Magna3 40-120 F.

Magna3 50-120 F.

Magna3 65-80F

Magna3 65-80F

Installation length

mm

180

180

220

250

280

340

340

Input signal

 

0-10V

0-10V

0-10V

0-10V

0-10V

0-10V

0-10V

free compression fP

m

9.0

6.2

5.0

3.5

3.2

2.5

2.0

connection
Heat source

customs

1 ½ "

1 ½ "

2 ½ "

2 ½ "

3 "

2 ½ "

3 "

Heat source flow rate VBW

* m³ / h *

7.6

10

14th

23

28.1

27.7

42.1

Pressure loss ΔpBW

Pa

22000

37000

25,000

55000

30820

21500

41500

Well pump M11*

 

Grundfos SP8A-3

Grundfos SP14A-3

Grundfos SP14A-3

Grundfos SP30-2

Grundfos SP30-2

Grundfos SP30-2

Grundfos SP46-2

free compression fP

m

10.5

13.3

11.5

12.0

11.7

13.4

13.3

* Suggestion for a well pump ** Control with 0 - 10V input signal absolutely necessary
Tab. 4.3: Overview table of the 2-compressor water / water heat pumps with generator circuit pumps (included in the scope of delivery of the heat pump) and the minimum required well pumps for W10 / W35 for standard systems with closed wells. The final definition of the well pump must be made in consultation with the well builder.

4.3.4.1 Stainless steel plate heat exchangers WTE 20 to WTE 40

 

Fig.4.2: WTE 20 - WTE 37

Fig.4.3: WTE 40

 

Device information stainless steel plate heat exchanger

mass and weight

unit

WTE 20

 

WTE 30

 

WTE 37

 

WTE 40

 

Number of plates

 

34

 

43

 

50

 

28

 

Effective area

2.69

 

3.44

 

4.03

 

3.90

 

volume

dm³

7th

 

9

 

11

 

9

 

Height [H]

mm

748

 

748

 

748

 

896

 

Width [B]

mm

200

 

200

 

200

 

283

 

Depth [L]

mm

270

 

320

 

420

 

437

 

Net weight

kg

67

 

71

 

76

 

132

 

Gross weight

kg

74

 

80

 

87

 

143

 

equipment

 

SZB 250

 

SZB 300

 

SZB 400

 

SZB 400

 

 

 

 

 

 

 

 

 

 

 

 

 

Secondary

Primary

Secondary

Primary

Secondary

Primary

Secondary

Primary

lot

m³ / h

4.5

5.8

7.0

8.0

8.5

9.3

11.0

11.0

Inlet temperature

° C

5.00

10.00

5.00

10.00

5.00

10.00

5.00

10.00

Outlet temperature

° C

8.41

7.00

8.07

7.00

7.92

7.00

7.58

7.00

Pressure drop

Pa

23740

30220

32110

37750

36630

37720

37610

32960

Transferred power

kW

18th

 

25th

 

29

 

33

 

Inlet port

 

F1

F3

F1

F3

F1

F3

F1

F3

Outlet port

 

F4

F2

F4

F2

F4

F2

F4

F2

Secondary connections

 

DN 32 (1 1/4 "AG)

 

 

 

 

 

DN 50 (2 "AG)

 

Connections primary

 

DN 32 (1 1/4 "AG)

 

 

 

 

 

DN 50 (2 "AG)

 

Plate material

 

0.5 mm AISI 316

 

 

 

 

 

0.4 mm AISI 316

 

Sealing material

 

NITRILE HT HANG ON (H) / 140

 

 

 

 

 

 

 

Tab.4.4: Technical data for screwed stainless steel plate heat exchangers WTE 20 - WTE 40

4.3.4.2 Stainless steel plate heat exchangers WTE 50 to WTE 130

 

Fig.4.4: WTE 50 - WTE 100

Fig.4.5: WTE 130

Device information stainless steel plate heat exchanger

mass and weight

unit

WTE 50

 

WTE 75

 

WTE 100

 

WTE 130

 

Number of plates

 

33

 

51

 

62

 

52

 

Effective area

4.65

 

7.35

 

9.00

 

11.14

 

volume

dm³

11

 

17th

 

21

 

31

 

Height [H]

mm

896

 

896

 

896

 

946

 

Width [B]

mm

283

 

283

 

283

 

395

 

Depth [L]

mm

437

 

537

 

537

 

443

 

Net weight

kg

136

 

150

 

160

 

253

 

Gross weight

kg

147

 

167

 

171

 

284

 

equipment

 

SZB 500

 

SZB 750

 

SZB 100

 

SZB 1300

 

 

 

 

 

 

 

 

 

 

 

 

 

Secondary

Primary

Secondary

Primary

Secondary

Primary

Secondary

Primary

lot

m³ / h

12.8

12.8

20.4

20.4

24.0

24.8

33.8

33.8

Inlet temperature

° C

5.00

10.00

5.00

10.00

5.00

10.00

5.00

10.00

Outlet temperature

° C

7.67

7.00

7.64

7.00

7.75

7.00

7.65

7.00

Pressure drop

Pa

38910

36400

38830

35380

39770

38960

40190

36720

Transferred power

kW

40

 

63

 

77

 

105

 

Inlet port

 

F1

F3

F1

F3

F1

F3

F1

F3

Outlet port

 

F4

F2

F4

F2

F4

F2

F4

F2

Secondary connections

 

DN 50 (2 "AG)

 

 

 

 

 

DN 65 (flange)

 

Connections primary

 

DN 50 (2 "AG)

 

 

 

 

 

DN 65 (flange)

 

Plate material

 

0.4 mm AISI 316

 

 

 

 

 

 

 

Sealing material

 

NITRILE HT HANG ON (H) / 140

 

 

 

 

 

 

 

Tab.4.5: Technical data of screwed stainless steel plate heat exchangers WTE 50 - WTE 130

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