I forgot to mention. In the September test, before the pump was hooked up, they measure 15.8 kg/hr (4.38g/s) consumption. Once connected to the E-Cat, it dropped to 13.76 kg/hr (3.8g/s), then at boiling, it dropped to 11.08 kg/hr (3.07g/s). This is just to demonstrate that the pump does not have consistent performance in the presence of any resistance. For calculations, we cannot rely on this flow rate, because the September/October tests may not entirely correlate. In the Mats Lewan report, the output of the primary side of the heat exchanger was measured at onyl .91 g/s and 1.9 g/s (when turned up for quenching). As the heat exchanger was probably receiving a water/steam mix, though, even these measurements may be unreliable.
From: robert.leguil...@hotmail.com To: vortex-l@eskimo.com Subject: RE: [Vo]:Rossi heat exchanger fitting / SOME flow data Date: Tue, 11 Oct 2011 13:02:37 -0500 The data from the September test is great, in this aspect. They did it right. They were filling the E-Cat from a reservoir, and after it was boiling, they gave us the net weight of water in the input reservoir at 21:07, then logged every time water was added, and provided us a final weight. Water flow inlet Added water during start up, from 18:30: 15640 + 9380 + 9473 + 9959 = 44452 grams. Remaining in the inlet reservoir when the temperature inside the E-cat reached 100°C at 21:07: 8431 grams. Consumed in 2:37 hours (2.62 hours): 36021 grams Flow during start-up: 13.76 kg/hour Added water from 21:07: 8431 + 10089 + 10460 + 6591 + 9960 = 45531 grams. Remaining in the inlet reservoir at 23:10: 22823 grams. Consumed in 2:03 hours (2.05 hours): 22708 grams Flow during boiling: 11.08 kg/hour. Total running time >100°C: 2:05 (2.08) hours Total flow >100 degrees (from 21:05): 23.0 kg IMPORTANT: In the September test, there is no reference to "increasing flow" at the end, they just turn the pump off. This begs the question if the September test had the pump running at full capacity. If so, the rate seen during Septembers operation of 11.08 kg/hr (3.1 g/sec) would be EVEN LOWER during the October test. We know for a fact that the October test, the pump was not running at full capacity, because they specifically stated that the increased the flow during quenching. Obviously, the pump does not put out consistent pressure, as seen in the September test. Was it slowed down for the October test? Was it harder to push through the heat exchanger, across the floor, under the doormat, then up into the drain, than the September test? If the placement of the thermocouples on the heat exchanger cause us to throw out that temperature data, and the E-Cat calorimetry is plagued with phase-change and unknown water flow, just where do we stand? Date: Tue, 11 Oct 2011 18:26:43 +0100 Subject: Re: [Vo]:Rossi heat exchanger fitting / SOME flow data From: robert.gulliver.l...@gmail.com To: vortex-l@eskimo.com Peristaltic pump NSF Model # CEP183-362N3 Serial # 060550065 Max output 12.0 liters/h Max press 1.50 bar So it was a maximum of 12 l/hr during cool-down, and if we take Lewan's numbers as a ratio -- 6 l/hr when stable. 12l/hr gives a maximum transfer rate of 8.8 kW -- close to the peak 7.6 kW recorded on the secondary. http://www.lmipumps.com/Files/lmi/Global/US-en/products/1713e.pdf If you know what the frequency is (the large thumping noise in all the videos about every second or so) then you can tell what the maximum flow rate is because the pump is only capable of deliverting 2ml per stroke.