IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at
IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at
IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask C1 Report, 31 October 2010 7 Steam jet chillers Clemens Pollerberg (Fraunhofer UMSICHT, Germany) 7.1 Brief description of the technology The Steam Jet Ejector Chiller (SJEC) is a thermo-mechanical chiller for cold generation. A refrigerant boils at a low pressure in the evaporator. The necessary heat of evaporation is provided by the water to be chilled. The vapour refrigerant is then compressed by a steam jet ejector to a higher pressure level and fed into a condenser. The driving energy of the steam jet ejector is supplied by motive steam, which can be generated by solar energy. The motive steam and vapour refrigerant are mixed in the steam jet ejector and both are liquefied in the condenser. The condensation takes place at a higher temperature than the ambient temperature, so that the heat from the condensation process can be rejected to the atmosphere. The condensate from the condenser is fed back to the evaporator and to the motive steam generator. Figure 33 depicts the principle of a solar driven SJEC. Figure 33: Principle sketch of a solar driven SJEC with water as working fluid and refrigerant. A SJEC can use water as the working fluid, which is used for generating the motive steam and as a refrigerant. In that case, an open process can be constructed without hydraulic separation between the solar collector and the SJEC or the chilled water network and the SJEC. The evaporator can be designed as a flash evaporator and the condenser as a direct contact condenser, such that both devices are basically vessels. The steam jet ejector consists of a motive steam nozzle, a mixing chamber and a diffuser. Thus the whole solar cooling system is simple in design and a high reliability of operation can be expected. Besides using water as both a working fluid and a refrigerant, different types of fluid have been discussed too. In particular, halocarbons, hydrocarbons and ammonia have been proposed for solar driven SJECs. The advantage of these proposed fluids is a reduction of the required temperature level of the driving heat, while still allowing adequate COP values to be reached. An overview of the possible types of fluid and an investigation of their applicability in a SJEC is given in [181]. SJECs in the higher cold capacity range are designed as two stage chillers and have several steam jet ejectors. In this case, the delivery rate of the ejectors could be different from each other in order to obtain a capacity control of the chiller by switching steam jet ejectors on/off. New approaches to increasing the efficiency of SJECs focus on the use of multiple ejectors in series and the use of two different types of fluid as working fluid and as refrigerant. page 69
IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask C1 Report, 31 October 2010 7.2 Main characteristics SJECs have a specific operational behaviour. The comparison between the reversible COP rev value and the real COP value of a SJEC points out this special operational behaviour, as shown in Figure 34. For this comparison, the COP is defined as the ratio of the cold energy produced in the evaporator Q E to the motive heat energy Q M required to operate the steam jet ejector, see equation 1. The reversible COP rev value is calculated according to equation 2 with the motive steam temperature T M (corresponding to the saturated steam pressure), the evaporator temperature T E and the condenser temperature T C . The evaporator temperature is 6 °C. COP COP Q& = Q& rev = E M ( T −T ) M T M C ⋅ ( T − T ) C T E E Equation 1 Equation 2 COP [-] 4 3 2 1 Motive steam temp.=120°C, rev Motive steam temp.=140°C, rev Motive steam temp.=160°C, rev Motive steam temp.=180°C, rev Motive steam temp.=120°C, real Motive steam temp.=140°C, real Motive steam temp.=160°C, real Motive steam temp.=180°C, real Evaporator temp. = 6°C 0 0 10 20 30 40 Condenser temp. [°C] Figure 34: COP value of SJEC, reversible and real machine. A higher motive steam temperature leads to a higher reversible COP rev value. Furthermore the reversible COP rev increases with decreasing condenser temperature. As a start, the COP value of a SJEC also increases with decreasing condenser temperature, but then remains constant below a certain condenser temperature. The reason for this behaviour is that the flow velocity in the steam jet ejector reaches supersonic speed and the mass flow through the ejector cannot be increased further. The comparison shows also that the motive steam temperature (corresponding to saturated steam pressure) can be reduced when the page 70
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<strong>IEA</strong> SHC Task 38 <strong>Solar</strong> Air Conditioning <strong>and</strong> Refriger<strong>at</strong>ion Subtask C1 Report, 31 October 2010<br />
7 Steam jet chillers<br />
Clemens Pollerberg (Fraunhofer UMSICHT, Germany)<br />
7.1 Brief description of the technology<br />
The Steam Jet Ejector Chiller (SJEC) is a thermo-mechanical chiller for cold gener<strong>at</strong>ion. A<br />
refrigerant boils <strong>at</strong> a low pressure in the evapor<strong>at</strong>or. The necessary he<strong>at</strong> of evapor<strong>at</strong>ion is<br />
provided by the w<strong>at</strong>er to be chilled. The vapour refrigerant is then compressed by a steam jet<br />
ejector to a higher pressure level <strong>and</strong> fed into a condenser. The driving energy of the steam<br />
jet ejector is supplied by motive steam, which can be gener<strong>at</strong>ed by solar energy. The motive<br />
steam <strong>and</strong> vapour refrigerant are mixed in the steam jet ejector <strong>and</strong> both are liquefied in the<br />
condenser. The condens<strong>at</strong>ion takes place <strong>at</strong> a higher temper<strong>at</strong>ure than the ambient<br />
temper<strong>at</strong>ure, so th<strong>at</strong> the he<strong>at</strong> from the condens<strong>at</strong>ion process can be rejected to the<br />
<strong>at</strong>mosphere. The condens<strong>at</strong>e from the condenser is fed back to the evapor<strong>at</strong>or <strong>and</strong> to the<br />
motive steam gener<strong>at</strong>or. Figure 33 depicts the principle of a solar driven SJEC.<br />
Figure 33: Principle sketch of a solar driven SJEC with w<strong>at</strong>er as working fluid <strong>and</strong> refrigerant.<br />
A SJEC can use w<strong>at</strong>er as the working fluid, which is used for gener<strong>at</strong>ing the motive steam<br />
<strong>and</strong> as a refrigerant. In th<strong>at</strong> case, an open process can be constructed without hydraulic<br />
separ<strong>at</strong>ion between the solar collector <strong>and</strong> the SJEC or the chilled w<strong>at</strong>er network <strong>and</strong> the<br />
SJEC. The evapor<strong>at</strong>or can be designed as a flash evapor<strong>at</strong>or <strong>and</strong> the condenser as a direct<br />
contact condenser, such th<strong>at</strong> both devices are basically vessels. The steam jet ejector<br />
consists of a motive steam nozzle, a mixing chamber <strong>and</strong> a diffuser. Thus the whole solar<br />
cooling system is simple in design <strong>and</strong> a high reliability of oper<strong>at</strong>ion can be expected.<br />
Besides using w<strong>at</strong>er as both a working fluid <strong>and</strong> a refrigerant, different types of fluid have<br />
been discussed too. In particular, halocarbons, hydrocarbons <strong>and</strong> ammonia have been<br />
proposed for solar driven SJECs. The advantage of these proposed fluids is a reduction of<br />
the required temper<strong>at</strong>ure level of the driving he<strong>at</strong>, while still allowing adequ<strong>at</strong>e COP values to<br />
be reached. An overview of the possible types of fluid <strong>and</strong> an investig<strong>at</strong>ion of their<br />
applicability in a SJEC is given in [181].<br />
SJECs in the higher cold capacity range are designed as two stage chillers <strong>and</strong> have several<br />
steam jet ejectors. In this case, the delivery r<strong>at</strong>e of the ejectors could be different from each<br />
other in order to obtain a capacity control of the chiller by switching steam jet ejectors on/off.<br />
New approaches to increasing the efficiency of SJECs focus on the use of multiple ejectors<br />
in series <strong>and</strong> the use of two different types of fluid as working fluid <strong>and</strong> as refrigerant.<br />
page 69