scholarly journals Direct Production of Butanol and Ethanol from Cane Sugar Factory Wastewater and Cellulosic Ethanol Pilot Plant Wastewater by Clostridium Beijerinckii CG1

2015 ◽  
Vol 79 ◽  
pp. 556-561 ◽  
Author(s):  
Jantarush Comwien ◽  
Nassapat Boonvithaya ◽  
Warawut Chulaluksananukul ◽  
Chompunuch Glinwong
2012 ◽  
pp. 756-761 ◽  
Author(s):  
Miroslav Hutnan ◽  
Štefan Tóth ◽  
Igor Bodík ◽  
Nina Kolesárová ◽  
Michal Lazor ◽  
...  

The possibility of joint treatment of spent sugar beet pulp and wastewater from a sugar factory was studied in this work. Works focused on processing of spent sugar beet pulp separately or together with other substrates can be found in the literature. In the case of some sugar factories, which have spare capacity in the anaerobic reactor on an anaerobic-aerobic wastewater treatment plant, joint processing of spent sugar beet pulp and wastewater from the sugar factory might be an interesting option. The results of the operation of a pilot plant of an anaerobic reactor with a capacity of 3.5 m3 are discussed. Operation of the pilot plant confirmed the possibility of cofermentation of these materials. The organic loading rate achieved in the anaerobic reactor was higher than 6 kg/(m3·d) (COD), while more than half of the load was provided by spent sugar beet pulp. The addition of sugar beet pulp decreased the concentration of ammonia nitrogen in the anaerobic reactor and it was even necessary to add nitrogen. However, the nitrogen content in sludge water depends on the C:N ratio in the processed sugar beet pulp, therefore this knowledge cannot be generalized. About 1.5 to 2-fold biogas production can be expected from the cofermentation of wastewater with sugar beet pulp in an anaerobic reactor, compared with the biogas production from just wastewater treatment.


2020 ◽  
pp. 607-612
Author(s):  
Bernard Coûteaux

This paper elaborates on the key solutions offered by De Smet Engineers & Contractors (DSEC) to optimize the efficiency of cane sugar producing and processing facilities. In order to meet customer needs, DSEC offers proprietary predictive models built using the latest versions of specialized software. These models allow factory managers to envision the whole picture of increased operational and capital efficiency before it becomes reality. An integrated energy model and the CAPEX/OPEX evaluation method are discussed as ways to estimate and optimize costs, both for new greenfield projects and revamping of existing factories. The models demonstrate that factory capacities can be successfully increased using equipment that is already available. Special attention is paid to crystallization and centrifugation process simulations and the potential improvement of the global energy balance. One case study shows the transformation of a beet sugar factory into a refinery to process raw cane sugar after beet crop season and the second case shows the integration of a refinery into a cane sugar factory. The primary focus of the article is optimization of the technological process through predictive modelling. DSEC’s suggested solutions, which lead to great improvements in a plant’s efficiency and its ability to obtain very low energy consumption, are discussed.


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.


2019 ◽  
pp. 705-713
Author(s):  
Gillian Eggleston ◽  
Jessica Gober ◽  
Duane Legendre ◽  
Eldwin St. Cyr

Measurement of sucrose losses across a cane sugar factory are notoriously difficult to measure directly or indirectly. Six loss trials were conducted at one factory across a Louisiana processing season; per trial, 40 samples were collected across four upstream and downstream unit processes. Sucrose losses were directly measured with gas chromatography using two equations based on (1) an increase in glucose/sucrose ratios on a RDS basis across a process, or a (2) a decrease in sucrose/RDS. When actual losses were <0.5%, eq. (2) did not detect losses due to the experimental error of the method being greater than the loss. Conversely, when high sucrose losses occurred, i.e., >0.5%, sucrose losses based on eq. (1) were lower than those based on eq. (2), because concomitant acid degradation of glucose occurred. Mean season losses were 2.56% equivalent to 4.89 lbs sucrose lost per short ton of cane and USD1,404,000, with values being much higher than previously reported. Mean losses were 2%, 24.8%, 58.6%, and 14.8% across the MJ tank, clarifier, two pre-evaporators (in series), and from the pre-evaporators to the final evaporator, respectively. 53% of total season losses occurred in early season when the cane quality was worst.


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