Impeller design assisted by physical modeling and pilot plant trials

2016 ◽  
Vol 236 ◽  
pp. 1-8 ◽  
Author(s):  
M. Hernández-Hernández ◽  
J.L. Camacho-Martínez ◽  
C. González-Rivera ◽  
M.A. Ramírez-Argáez
Processes ◽  
2021 ◽  
Vol 9 (4) ◽  
pp. 586
Author(s):  
Eddy Plasquy ◽  
José María García Martos ◽  
María del Carmen Florido Fernández ◽  
Rafael Rubén Sola-Guirado ◽  
Juan Francisco García Martín

Harvesting at high temperatures and bulk transport can negatively influence the quality of olives and lead to undesirable alterations in the extracted oil. Cooling the fruit in the field would be the most logical solution, but it means that the olives arrive too cold at the mill for immediate processing. In this work, the use of warm water in the washing tub to warm up the fruit before grinding instead of flash heat treatment on the paste was assessed in two experiments. In the first one, at the laboratory level, the temperature after milling was determined in three olive cultivars, previously stored at 5 or 10 °C, and then submerged at different water temperatures (25, 30, and 35 °C) for 15, 30, 45, and 60 s. In the second one, two batches of olives were cooled in the field at 5 °C and then conditioned with washing water to obtain a paste at the entrance of the pilot plant malaxer at 27 °C. The temperature of the olives was measured at five points from the discharging up to their entering, as paste, into the malaxer. The results demonstrated the feasibility of the method as the temperature of the ground olives was kept at the desired temperature (28 ± 1 °C). The trials highlight the potential for automating an even more precise adjustment of the temperature of the olives before milling once the washing tub is equipped with a safe heating system.


1992 ◽  
Vol 25 (10) ◽  
pp. 339-350 ◽  
Author(s):  
D. M. Meadows ◽  
S. Wadley ◽  
C. A. Buckley

The recovery of brine from the regeneration effluent from cane sugar Liquor decolourising ion exchange resin by means of nano filtration has been investigated on a Laboratory and pilot plant scale. This effluent is produced at 80°C and contains up to 110 g/ℓ of sodium chloride and up to 6 g/ℓ (as total carbon) of organic matter. The SelRO MPT-30 membrane was selected for the pilot plant trials, which were carried out at 3 MPa and 45 °C or 60 °C. Point retention values ranged from (-2) to 15 % for sodium chloride and from 71 to 93 % for total carbon. Final water recoveries between 69 and 83 % were investigated. The sodium chloride recovery ranged from 64 to 81 % and the total carbon removal ranged from 79 to 89 %. Based on experiments using the salt-rich fraction of the effluent and a water balance over the regeneration system, it was calculated that a 30 % reduction in effluent volume and a 60 % reduction in salt consumption could be achieved. In the tests carried out so far, the use of the recovered brine in the regeneration of pilot resin columns did not lower the decolourising capacity of the resin.


2016 ◽  
Vol 70 (2) ◽  
pp. 411-419 ◽  
Author(s):  
Venugopal Tammishetti ◽  
Dharmendr Kumar ◽  
Beena Rai ◽  
Pradip ◽  
Vishal Shukla ◽  
...  

1993 ◽  
Vol 7 (4) ◽  
pp. 333-342 ◽  
Author(s):  
G. S. TAYLOR ◽  
P. HILLIS ◽  
I. WALKER
Keyword(s):  

2014 ◽  
Vol 49 (16) ◽  
pp. 2449-2458 ◽  
Author(s):  
Colin A. Scholes ◽  
Abdul Qader ◽  
Geoff W. Stevens ◽  
Sandra E. Kentish
Keyword(s):  
Flue Gas ◽  

2007 ◽  
Vol 2 (1) ◽  
Author(s):  
Bernd Heinzmann ◽  
Gerd Engel

Improved sludge disposal can be achieved by intensified digestion. With the reduction of the hydraulic retention time and by higher dried solid matter of the sludge, the volume load increases. In the WWTP Waßmannsdorf the digestion could be intensified by higher DSM of the mixed sludge. Furthermore, by application of a two-stage high rate digestion process in first tests in 2002 a degree of degradation of around 50 % organic DSM was achieved. A high organic volume load of around 3.2 kg/m3 per day and a degradation rate of around 50 % were results of first pilot plant trials over a time period of more than 3 month with the two-stage high rate digestion process without usage of a rotating membrane disk filter and showed a stable and safe operation. By using the RMD in the next phase of the pilot plant trials more water will be extracted from the digested sludge and so the digestion time can be extended and the organic volume load can be increased, in order to achieve further improvements (degree of degradation and improved gas production). Furthermore, there is a high potential for P-recovery in the highly digested (mineralised) sludge. First trials show in principle that precipitated MAP could be separated by using the hydro-cyclone technique.


1987 ◽  
Vol 4 (2) ◽  
pp. 87-89
Author(s):  
E. Forssberg ◽  
T. Nordquist

2016 ◽  
Vol 306 ◽  
pp. 471-483 ◽  
Author(s):  
Daniel Woldemariam ◽  
Alaa Kullab ◽  
Uwe Fortkamp ◽  
Jörgen Magner ◽  
Hugo Royen ◽  
...  

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