The effect of angiotensin II on intracellular pH is mediated by AT(1) receptor translocation

The effect of ANG II on intracellular pH (pH(i)) recovery rate and AT(1) receptor translocation was investigated in transfected MDCK cells. The pHi recovery rate was evaluated by fluorescence microscopy using the fluorescent probe BCECF-AM. The human angiotensin II receptor isoform 1 (hAT(1)) translocation was analyzed by immunofluorescence and confocal microscope. Our data show that transfected cells in control situation have a pHi recovery rate of 0.219 +/- 0.017 pH U/min (n = 11). This value was similar to nontransfected cells [0.211 +/- 0.009 pH U/min (n = 12)]. Both values were significantly increased with ANG II (10(-9) M) but not with ANG II (10(-6) M). Losartan (10(-7) M) and dimethyl-BAPTA-AM (10(-7) M) decreased significantly the stimulatory effect of ANG II (10(-9) M) and induced an increase in Na+/H+ exchanger 1 (NHE-1) activity with ANG II (10(-6) M). Immunofluorescence studies indicated that in control situation, the hAT(1) receptor was predominantly expressed in cytosol. However, it was translocated to plasma membrane with ANG II (10(-9) M) and internalized with ANG II (10(-6) M). Losartan (10(-7) M) induced hAT(1) translocation to plasma membrane in all studied groups. Dimethyl-BAPTA-AM (10(-7) M) did not change the effect of ANG II (10(-9) M) on the hAT(1) receptor distribution but induced its accumulation at plasma membrane in cells treated with ANG II (10(-6) M). With ionomycin (10(-6) M), the receptor was accumulated in cytosol. The results indicate that, in MDCK cells, the effect of ANG II on NHE-1 activity is associated with ligand binding to AT(1) receptor and intracellular signaling events related to AT(1) translocation.

NHE1, NHE2, and NHE4 contribute to regulation of cell pH in T84 colon cancer cells

The isoforms of the Na+/H+ exchanger present in T84 human colon cells were identified by functional and molecular methods. Cell pH was measured by fluorescence microscopy using the probe BCECF. Based on the pH recovery after an ammonium pulse and determination of buffering capacity of these cells, the rate of H+ extrusion (J(H)) was 3.68 mM/min. After the use of the amiloride derivative HOE-694 at 25 mu M, which inhibits the isoforms NHE1 and NHE2, there remained 43% of the above transport rate, the nature of which was investigated. Evidence of the presence of NHE1, NHE2, and NHE4 was obtained by reverse transcriptase polymerase chain reaction (RT-PCR) (mRNA) and Western blot. There was no decrease of J(H) by the NHE3 inhibitor S3226 (1 mu M) and no evidence of this isoform by RT-PCR was found. The following functional evidence for the presence of NHE4 was obtained: 25 mu M EIPA abolished J(H) entirely, but NHE4 was not inhibited at 10 mu M; substitution of Na by K increased the remainder, a property of NHE4; hypertonicity also increased this fraction of J(H). Cl--dependent NHE was not detected: in 0 Cl- solutions J(H) was increased and not reduced. In 0 Cl- cell volume decreased significantly, which was abolished by the Cl- channel blocker NPPB, indicating that the 0 Cl- effect was because of reduction of cell volume. In conclusion, T84 human colon cells contain three isoforms of the Na+/H+ exchanger, NHE1, NHE2, and NHE4, but not the Cl-dependent NHE.

Glucose-Induced Regulation of NHEs Activity and SGLTs Expression Involves the PKA Signaling Pathway

The effect of glucose on the intracellular pH (pH(i)) recovery rate (dpH(i)/dt) and Na(+)-glucose transporter (SGLT) localization was investigated in HEK-293 cells, a cell line that expresses endogenous NHE1, NHE3, SGLT1, and SGLT2 proteins. The activity of the Na(+)/H(+) exchangers (NHEs) was evaluated by using fluorescence microscopy. The total and membrane protein expression levels were analyzed by immunoblotting. In cells cultivated in 5 mM glucose, the pH(i) recovery rate was 0.169 +/- A 0.020 (n = 6). This value did not change in response to the acute presence of glucose at 2 or 10 mM, but decreased with 25 mM glucose, an effect that was not observed with 25 mM mannitol. Conversely, the chronic effect of high glucose (25 mM) increased the pH(i) recovery rate (similar to 40%, P < 0.05), without changes in the total levels of NHE1, NHE3, or SGLT1 expression, but increasing the total cellular (similar to 50%, P < 0.05) and the plasma membrane (similar to 100%, P < 0.01) content of SGLT2. Treatment with H-89 (10(-6) M) prevented the stimulatory effect of chronic glucose treatment on the pH(i) recovery rate and SGLT2 expression in the plasma membrane. Our results indicate that the effect of chronic treatment with a high glucose concentration is associated with increased NHEs activity and plasma membrane expression of SGLT2 in a protein kinase A-dependent way. The present results reveal mechanisms of glucotoxicity and may contribute to understanding the diabetes-induced damage of this renal epithelial cell.

Acid-base transport by the renal distal nephron

The functional versatility of the distal nephron is mainly due to the large cytological heterogeneity of the segment. Part of Na(+) uptake by distal tubules is dependent on Na(+)/H(+). exchanger 2 (NHE2), implicating a role of distal convoluted cells also in acid-base homeostasis. In addition, intercalated (IC) cells expressed in distal convoluted tubules, connecting tubules and collecting ducts are involved in the final regulation of acid-base excretion. IC cells regulate acid-base handling by 2 main transport proteins, a V-type H(+)-ATPase and a Cl/HCO(3)(-) exchanger, localized at different membrane domains. Type A IC cells are characterized by a luminal H(+)-ATPase in series with a basolateral Cl/HCO(3)(-) exchanger, the anion exchanger AE1. Type B IC cells mediate HCO(3)(-) secretion through the apical Cl(-)/HCO(3)(-) exchanger pendrin in series with a H(+)-ATPase at the basolateral membrane. Alternatively, H(+)/K(+)-ATPases have also been found in several distal tubule cells, particularly in type A and B IC cells. All of these mechanisms are finely regulated, and mutations of 1 or more proteins ultimately lead to expressive disorders of acid-base balance.

Role of CFTR and ClC-5 in Modulating Vacuolar H(+)-ATPase Activity in Kidney Proximal Tubule

Background/Aims: It has been widely accepted that chloride ions moving along chloride channels act to dissipate the electrical gradient established by the electrogenic transport of H(+) ions performed by H(+)-ATPase into subcellular vesicles. Largely known in intracellular compartments, this mechanism is also important at the plasma membrane of cells from various tissues, including kidney. The present work was performed to study the modulation of plasma membrane H(+)-ATPase by chloride channels, in particular, CFTR and ClC-5 in kidney proximal tubule. Methods and Results: Using in vivo stationary microperfusion, it was observed that ATPase-mediated HCO(3)(-) reabsorption was significantly reduced in the presence of the Cl(-) channels inhibitor NPPB. This effect was confirmed in vitro by measuring the cell pH recovery rates after a NH(4)Cl pulse in immortalized rat renal proximal tubule cells, IRPTC. In these cells, even after abolishing the membrane potential with valinomycin, ATPase activity was seen to be still dependent on Cl(-). siRNA-mediated CFTR channels and ClC-5 chloride-proton exchanger knockdown significantly reduced H(+)-ATPase activity and V-ATPase B2 subunit expression. Conclusion: These results indicate a role of chloride in modulating plasma membrane H(+)-ATPase activity in proximal tubule and suggest that both CFTR and ClC-5 modulate ATPase activity. Copyright (C) 2010 S. Karger AG, Basel

Effect of renoguanylin on hydrogen/bicarbonate ion transport in rat renal tubules

Renoguanylin (REN) is a recently described member of the guanylin family, which was first isolated from eels and is expressed in intestinal and specially kidney tissues. In the present work we evaluate the effects of REN on the mechanisms of hydrogen transport in rat renal tubules by the stationary microperfusion method. We evaluated the effect of 1 mu M and 10 mu M of renoguanylin (REN) on the reabsorption of bicarbonate in proximal and distal segments and found that there was a significant reduction in bicarbonate reabsorption. In proximal segments, REN promoted a significant effect at both 1 and 10 mu M concentrations. Comparing control and REN concentration of 1 mu M, JHCO(3)(-) . nmol cm(-2) s(-1) -1,76 +/- 0.11(control) x 1,29 +/- 0,08(REN) 10 mu m: P<0.05, was obtained. In distal segments the effect of both concentrations of REN was also effective, being significant e.g. at a concentration of 1 mu M (JHCO(3)(-), nmol cm(-2) s(-1) -0.80 +/- 0.07(control) x 0.60 +/- 0.06(REN) 1 mu m; P<0.05), although at a lower level than in the proximal tubule. Our results suggest that the action of REN on hydrogen transport involves the inhibition of Na(+)/H(+) exchanger and H(+)-ATPase in the luminal membrane of the perfused tubules by a PKG dependent pathway. (c) 2009 Elsevier B.V. All rights reserved.

Mechanisms underlying the long-term regulation of NHE3 by parathyroid hormone

The activity of the Na(+)/H(+) exchanger NHE3 is regulated by a number of factors including parathyroid hormone (PTH). In the current study, we used a renal epithelial cell line, the opossum kidney (OKP) cell, to elucidate the mechanisms underlying the long-term effects of PTH on NHE3 transport activity and expression. We observed that NHE3 activity was reduced 6 h after addition of PTH, and this reduction persisted almost unaltered after 24 h. The decrease in activity was associated with diminished NHE3 cell surface expression at 6, 16, and 24 h after PTH addition, total cellular NHE3 protein at 16 and 24 h, and NHE3 mRNA abundance at 24 h. The lower levels of NHE3 mRNA were associated to a small, but significant, decrease in mRNA stability. Additionally, by analyzing the rat NHE3 gene promoter activity in OKP cells, we verified that the regulatory region spanning the segment -152 to +55 was mildly reduced under the influence of PTH. This effect was completely abolished by the presence of the PKA inhibitor KT 5720. In conclusion, long-term exposure to PTH results in reduction of NHE3 mRNA levels due to a PKA-dependent inhibitory effect on the NHE3 promoter and a small reduction of mRNA half-life, and decrease in the total amount of protein which is preceded by endocytosis of the apical surface NHE3. The decreased NHE3 expression is likely to be responsible for the reduction of sodium, bicarbonate, and fluid reabsorption in the proximal tubule consistently perceived in experimental models of PTH disorders.

Dipeptidyl peptidase IV inhibition attenuates blood pressure rising in young spontaneously hypertensive rats

Objectives The present study aimed to assess the effect of the specific dipeptidyl peptidase IV (DPPIV) inhibitor sitagliptin on blood pressure and renal function in young prehypertensive (5-week-old) and adult spontaneously hypertensive rats (SHRs; 14-week-old). Methods Sitagliptin (40 mg/kg twice daily) was given by oral gavage to young (Y-SHR + IDPPIV) and adult (A-SHR R IDPPIV) SHRs for 8 days. Kidney function was assessed daily and compared with age-matched vehicle-treated SHR (Y-SHR and A-SHR) and with normotensive Wistar-Kyoto rats (Y-WKY and A-WKY). Arterial blood pressure was measured in these animals at the end of the experimental protocol. Additionally, Na(+)/H(+) exchanger isoform 3 (NHE3) function and expression in microvilli membrane vesicles were assessed in young animals. Results Mean arterial blood pressure of Y-SHR + IDPPIV was significantly lower than that of Y-SHR (104 +/- 3 vs. 123 +/- 5 mmHg, P < 0.01) and was similar to Y-WKY (94 +/- 4 mmHg, P > 0.05). Compared to Y-SHR, Y-SHR + IDPPIV exhibited enhanced cumulative urinary flow and sodium excretion and decreased NHE3 activity and expression in proximal tubule microvilli. In the A-SHR, sitagliptin treatment had no significant effect on either renal function or arterial blood pressure. Conclusion Our data suggest that DPPIV inhibition attenuates blood pressure rising in young prehypertensive SHRs, partially by inhibiting NHE3 activity in renal proximal tubule. J Hypertens 29:520-528 (C) 2011 Wolters Kluwer Health vertical bar Lippincott Williams & Wilkins.

Determination of amino acids by capillary electrophoresis-electrospray ionization-mass spectrometry: An evaluation of different protein hydrolysis procedures

In this work, a CE equipment, online hyphenated to an IT MS analyzer by a linear sheath liquid interface promoting ESI, was used to develop a method for quantitative determination of amino acids. Under appropriate conditions (BGE composition, 0.8% HCOOH, 20% CH(3)OH; sheath liquid composition, 0.8% HCOOH, 60% methanol; V(ESI), +4.50 W), analytical curves of all amino acids from 3 to 80 mg/L were recorded presenting acceptable linearity (r > 0.99). LODs in the range of 16-172 mu mol/L were obtained. BSA, a model protein, was submitted to different hydrolysis procedures (classical acid and basic, and catalyzed by the H(+) form of a cation exchanger resin) and its amino acid profiles determined. In general, the resin-mediated hydrolysis yields were overall similar or better than those obtained by classical acid or basic hydrolysis. The resulting experimental-to-theoretical BSA concentration ratios served as correction factors for the quantitation of amino acids in Brazil nut resin generated hydrolysates.

Identifiering av parametrar till ackumulatortanken Solus1050 fr��n consolar - en metodbeskrivning

This report describes the work done creating a computer model of a kombi tank from Consolar. The model was created with Presim/Trnsys and Fittrn and DF were used to identify the parameters. Measurements were carried out and were used to identify the values of the parameters in the model. The identifications were first done for every circuit separately. After that, all parameters are normally identified together using all the measurements. Finally the model should be compared with other measurements, preferable realistic ones. The two last steps have not yet been carried out, because of problems finding a good model for the domestic hot water circuit.The model of the domestic hot water circuit give relatively good results for low flows at 5 l/min, but is not good for higher flows. In the report suggestions for improving the model are given. However, there was not enough time to test this within the project as much time was spent trying to solve problems with the model crashing. Suggestions for improving the model for the domestic circuit are given in chapter 4.4. The improved equations that are to be used in the improved model are given by equation 4.18, 4.19 and 4.22.Also for the boiler circuit and the solar circuit there are improvements that can be done. The model presented here has a few shortcomings, but with some extra work, an improved model can be created. In the attachment (Bilaga 1) is a description of the used model and all the identified parameters.A qualitative assessment of the store was also performed based on the measurements and the modelling carried out. The following summary of this can be given: Hot Water PreparationThe principle for controlling the flow on the primary side seems to work well in order to achieve good stratification. Temperatures in the bottom of the store after a short use of hot water, at a coldwater temperature of 12&#176;C, was around 28-30&#176;C. This was almost independent of the temperature in the store and the DHW-flow.The measured UA-values of the heat exchangers are not very reliable, but indicates that the heat transfer rates are much better than for the Conus 500, and in the same range as for other stores tested at SERC.The function of the mixing valve is not perfect (see diagram 4.3, where Tout1 is the outlet hot water temperature, and Tdhwo and Tdhw1 is the inlet temperature to the hot and cold side of the valve respectively). The outlet temperature varies a lot with different temperatures in the storage and is going down from 61&#176;C to 47&#176;C before the cold port is fully closed. This gives a problem to find a suitable temperature setting and gives also a risk that the auxiliary heating is increased instead of the set temperature of the valve, when the hot water temperature is to low.Collector circuitThe UA-value of the collector heat exchanger is much higher than the value for Conus 500, and in the same range as the heat exchangers in other stores tested at SERC.Boiler circuitThe valve in the boiler circuit is used to supply water from the boiler at two different heights, depending on the temperature of the water. At temperatures from the boiler above 58.2&#176;C, all the water is injected to the upper inlet. At temperatures below 53.9&#176;C all the water is injected to the lower inlet. At 56&#176;C the water flow is equally divided between the two inlets. Detailed studies of the behaviour at the upper inlet shows that better accuracy of the model would have been achieved using three double ports in the model instead of two. The shape of the upper inlet makes turbulence, that could be modelled using two different inlets. Heat lossesThe heat losses per m3 are much smaller for the Solus 1050, than for the Conus 500 Storage. However, they are higher than those for some good stores tested at SERC. The pipes that are penetrating the insulation give air leakage and cold bridges, which could be a major part of the losses from the storage. The identified losses from the bottom of the storage are exceptionally high, but have less importance for the heat losses, due to the lower temperatures in the bottom. High losses from the bottom can be caused by air leakage through the insulation at the pipe connections of the storage.

Combined solar and pellet heating systems for single-family houses : How to achieve decreased electricity usage, increased system efficiency and increased solar gains

In Sweden, there are about 0.5 million single-family houses that are heated by electricity alone, and rising electricity costs force the conversion to other heating sources such as heat pumps and wood pellet heating systems. Pellet heating systems for single-family houses are currently a strongly growing market. Future lack of wood fuels is possible even in Sweden, and combining wood pellet heating with solar heating will help to save the bio-fuel resources. The objectives of this thesis are to investigate how the electrically heated single-family houses can be converted to pellet and solar heating systems, and how the annual efficiency and solar gains can be increased in such systems. The possible reduction of CO-emissions by combining pellet heating with solar heating has also been investigated. Systems with pellet stoves (both with and without a water jacket), pellet boilers and solar heating have been simulated. Different system concepts have been compared in order to investigate the most promising solutions. Modifications in system design and control strategies have been carried out in order to increase the system efficiency and the solar gains. Possibilities for increasing the solar gains have been limited to investigation of DHW-units for hot water production and the use of hot water for heating of dishwashers and washing machines via a heat exchanger instead of electricity (heat-fed appliances). Computer models of pellet stoves, boilers, DHW-units and heat-fed appliances have been developed and the parameters for the models have been identified from measurements on real components. The conformity between the models and the measurements has been checked. The systems with wood pellet stoves have been simulated in three different multi-zone buildings, simulated in detail with heat distribution through door openings between the zones. For the other simulations, either a single-zone house model or a load file has been used. Simulations were carried out for Stockholm, Sweden, but for the simulations with heat-fed machines also for Miami, USA. The foremost result of this thesis is the increased understanding of the dynamic operation of combined pellet and solar heating systems for single-family houses. The results show that electricity savings and annual system efficiency is strongly affected by the system design and the control strategy. Large reductions in pellet consumption are possible by combining pellet boilers with solar heating (a reduction larger than the solar gains if the system is properly designed). In addition, large reductions in carbon monoxide emissions are possible. To achieve these reductions it is required that the hot water production and the connection of the radiator circuit is moved to a well insulated, solar heated buffer store so that the boiler can be turned off during the periods when the solar collectors cover the heating demand. The amount of electricity replaced using systems with pellet stoves is very dependant on the house plan, the system design, if internal doors are open or closed and the comfort requirements. Proper system design and control strategies are crucial to obtain high electricity savings and high comfort with pellet stove systems. The investigated technologies for increasing the solar gains (DHW-units and heat-fed appliances) significantly increase the solar gains, but for the heat-fed appliances the market introduction is difficult due to the limited financial savings and the need for a new heat distribution system. The applications closest to market introduction could be for communal laundries and for use in sunny climates where the dominating part of the heat can be covered by solar heating. The DHW-unit is economical but competes with the internal finned-tube heat exchanger which is the totally dominating technology for hot water preparation in solar combisystems for single-family houses.

Fj��rrv��rmedrivna vitvaror : Erfarenheter fr��n utveckling, installationer och kostnadsber��kningar

V��rmedrivna vitvaror eller HWC-maskiner som de kallas av tillverkaren v��rms med varmt vatten fr��n en cirkulerande krets via en v��rmev��xlare inbyggd i maskinen, till skillnad fr��n konventionella maskiner som v��rms med el. Denna teknik skall inte f��rv��xlas med maskiner som ��r anslutna till varmvattenledningen och fylls p�� med varmt vatten och som d��rmed begr��nsas till disk- och tv��tt. Syftet med fj��rrv��rmedrivna vitvaror ��r allts�� att anv��nda fj��rrv��rme, som har l��gre kvalitet och pris ��n elenergi f��r uppv��rmning och torkning och p�� s�� s��tt spara el och ut��ka fj��rrv��rmeunderlaget. En j��mf��relse av koldioxidutsl��pp och prim��renergianv��ndning mellan konventionella vitvaror och fj��rrv��rmedrivna vitvaror visar att b��de koldioxidutsl��pp och prim��renergianv��ndning blir l��gre f��r fj��rrv��rmedrivna vitvaror om biobr��nsle anses koldioxidneutralt och den el som ers��tts ��r producerad i kolkraftverk eller gaskombikraftverk. �� Denna rapport beskriver utveckling och kommersialisering av v��rmedrivna vitvaror (disk- och tv��ttmaskiner samt torktumlare och torksk��p) och hur de kan anslutas mot fj��rrv��rmesystem i olika systeml��sningar. Dessutom har de energim��ssiga och ekonomiska f��ruts��ttningarna f��r tekniken unders��kts. Erfarenheterna fr��n f��ltprovning ��r dock mycket begr��nsade, eftersom de byggen d��r f��lttesterna skulle ske f��rsenades. Under 2013 f��rdigst��lls ett flerbostadshus med v��rmedrivna vitvaror i 160 l��genheter i V��ster��s. �� De utvecklade maskinernas v��rmeanv��ndning som andel av total energianv��ndning vid 60 graders framledningstemperatur har uppm��tts till ca 50 % f��r diskmaskinen, 67 % f��r tv��ttmaskinen, 80 % f��r torktumlaren och 93 % f��r torksk��pet. I det studerade flerbostadshuset av passivhusstandard uppg��r lasten fr��n v��rmedrivna vitvaror komfortgolvv��rme och handdukstorkar till upp mot 30 % av husets totala v��rmeanv��ndning. F��r sm��hus ��r motsvarande siffra upp mot 20 %. Att anv��nda fj��rrv��rme ist��llet f��r elv��rme till dessa installationer som normalt ��r elv��rmda kan allts minska elbehovet betydligt i l��genergibebyggelse vilket ocks�� minskar b��de koldioxidutsl��ppen och prim��renergianv��ndningen. �� Ekonomiska analyser har genomf��rts f��r tv�� olika systemkoncept (separat vitvarukrets och V��ster��smodellen) f��r nybyggda sm��husomr��den och flerfamiljshus d��r fj��rrv��rme inte bara anv��nds till vitvaror utan ocks�� till handdukstorkar och komfortgolvv��rme. De ekonomiska analyserna visar att V��ster��smodellen ��r den mest ekonomiskt intressanta systeml��sningen med v��rmedrivna vitvaror, handdukstork och komfortgolvv��rme. I flerfamiljshus kan den vara konkurrenskraftig mot de elv��rmda alternativen (konventionellt system med eldrivna vitvaror, komfortgolvv��rme och handdukstorkar) om prisskillnaden mellan el och fj��rrv��rme ��r st��rre ��n 0,7 kr/kWh. En parameterstudie visar att kapitalkostnaden blir ganska h��g j��mf��rt med energikostnaden, vilket betyder att l��ng livsl��ngd och m��nga cykler ��r viktigt f��r att f��rb��ttra de ekonomiska f��ruts��ttningarna f��r v��rmedrivna vitvaror. F��r passiva sm��hus blir kostnaden f��r V��ster��smodellen med v��rmedrivna vitvaror, handdukstork och komfortgolvv��rme likv��rdig med de elv��rmda alternativen vid energiprisskillnader p�� 0,7 kr/kWh inklusive moms, medan det kr��vs prisskillnader p�� 0,9 kr/kWh inklusive moms f��r normalisolerade sm��husomr��den. �� Sammanfattningsvis kan s��gas att i kommuner med ett konkurrenskraftigt fj��rrv��rmepris finns det viss l��nsamhet f��r hela konceptet enligt V��ster��smodellen med v��rmedrivna vitvaror, komfortgolvv��rme, och handdukstorkar. Om man d��remot ser p�� konkurrensen f��r enskilda vitvaror ��r det fr��mst torktumlaren som ��r konkurrenskraftig i bost��der. M��lpriset p�� 1000 kr extra f��r v��rmedrift har inte kunnat uppn��s inom projektet f��r diskmaskiner och tv��ttmaskiner. Det kr��vs l��gre priser och l��ga anslutningskostnader f��r att r��kna hem diskmaskinen och tv��ttmaskinen som enskilda komponenter. �� V��rmedrivna tv��ttmaskiner och torktumlare ��r konkurrenskraftiga i flerfamiljstv��ttstugor. Speciellt i de fall d��r bel��ggningen ��r god och flera maskiner delar p�� anslutningskostnaden till fj��rrv��rmecentralen kan v��rmedrift bli riktigt l��nsam. Torksk��pens konkurrenskraft har inte kunnat utv��rderas, d�� priset ��nnu inte fastst��llts. Att anv��nda VVC-systemet f��r v��rmedistribution till v��rmedrivna vitvaror kan vara mycket intressant, men det kr��ver att legionellaproblematiken kan l��sas. I nul��get finns ingen l��sning som uppfyller formuleringarna i boverkets byggregler. Ett annat distributionss��tt som kan vara intressant, men som inte unders��kts i studien ��r att anv��nda VVC f��r varmvattendistribution och en gemensam radiator- och vitvarukrets med konstant framledningstemperatur. Den akt��r som f��rv��ntas ha st��rst ekonomiskt intresse av att tekniken implementeras ��r sannolikt fj��rrv��rmebolagen som f��r s��lja mer v��rme och det ligger d��rmed fr��mst p�� deras ansvar att marknadsf��ra tekniken i m��tet med sina kunder.

Replacing Finned Copper withCorrugated Stainless Steel, forthe Heat Exchangers of a SolarCombisystem Store : Performance and EconomicEvaluation

The importance of investigating cost reduction in materials and components for solar thermal systems is crucial at the present time. This work focuses on the influence of two different heat exchangers on the performance of a solar thermal system. Both heat exchangers studied are immersed helically coiled, one made with corrugated stainless steel tube, and the other made with finned copper tube with smooth inner surface.A test apparatus has been designed and a simple test procedure applied in order to study heat transfer characteristics and pressure drop of both coils. Thereafter, the resulting experimental data was used to perform a parameter identification of the heat exchangers, in order to obtain a TRNSYS model with its corresponding numerical expression. Also a representative small-scale combisystem model was designed in TRNSYS, in order to study the influence of both heat exchangers on the solar fraction of the system, when working at different flow rates.It has been found that the highest solar fraction is given by the corrugated stainless steel coil, when it works at the lowest flow rate (100 l/hr). For any higher flow rate, the studied copper coil presents a higher solar fraction. The advantageous low flow performance of stainless steel heat exchanger turns out to be beneficial for the particular case of solar thermal systems, where it is well known that low flow collector loops lead to enhanced store stratification, and consequently higher solar fractions.Finally, an optimization of the stainless steel heat exchanger length is carried out, according to economic figures. For the given combisystem model and boundary conditions, the optimum length value is found between 10 and 12 m.

Simulation study of cascade heat pump for solar combisystems

This paper focuses on the study of cascade heat pump systems in combination with solar thermal for the production of hot water and space heating in single family houses with relatively high heating demand. The system concept was developed by Ratiotherm GmbH and simulated with TRNSYS 17. The basic cascade system uses the heat pump and solar collectors in parallel operation while a further development is the inclusion of an intermediate store that enables the possibility of serial/parallel operation and the use of low temperature solar heat. Parametric studies in terms of compressor size, refrigerant pair and size of intermediate heat exchanger were carried out for the optimization of the basic system. The system configurations were simulated for the complete year and compared to a reference of a solar thermal system combined with an air source heat pump. The results show ~13% savings in electricity use for all three cascade systems compared to the reference. However, the complexity of the systems is different and thus higher capital costs are expected.

Influence of hydraulics and control of thermal storage in solar assisted heat pump combisystems

This paper studies the influence of hydraulics and control of thermal storage in systems combined with solar thermal and heat pump for the production of warm water and space heating in dwellings. A reference air source heat pump system with flat plate collectors connected to a combistore was defined and modeled together with the IEA SHC Task 44 / HPP Annex 38 (T44A38) ���Solar and Heat Pump Systems��� boundary conditions of Strasbourg climate and SFH45 building. Three and four pipe connections as well as use of internal and external heat exchangers for DHW preparation were investigated as well as sensor height for charging of the DHW zone in the store. The temperature in this zone was varied to ensure the same DHW comfort was achieved in all cases. The results show that the four pipe connection results in 9% improvement in SPF compared to three pipe and that the external heat exchanger for DHW preparation leads to a 2% improvement compared to the reference case. Additionally the sensor height for charging the DHW zone of the store should not be too low, otherwise system performance is adversely affected