Seasonal chemical sucrose losses in upstream and downstream products at a cane sugar factory

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.

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.


In an earlier communication, Perman and Urry described the measurement, by a direct method, of the compressibility coefficients of aqueous solution of urea, cane sugar, potassium chloride, and calcium chloride, over a range temperatures and concentrations. Their work was over the pressure range 0-200 atmospheres excess pressure. They were able to apply their together with other data obtained by their co-workers, to an extension Porter's theory of compressible solutions, and thus obtained values for osmotic pressures of those solutions which agreed very well with the obtained by more direct methods. The present work is a continuation of this and subsequent work (unpublished) by these authors. It was intended, especially, to investigate the effect of nature of the solute molecule upon the compressibility, and, for this reason the choice of solutes was particularly important. A number of series chemically related compounds were used where only one part of the mole varied in a progressive manner from substance to substance. In series there was no chemical relationship, but the members had the empirical formula and their molecular weights were therefore simple multi of each other.


2008 ◽  
Vol 58 (1) ◽  
pp. 143-151 ◽  
Author(s):  
Ruikang Hu ◽  
Lifeng Zhang ◽  
Zhaoguang Yang

N-nitrosodimethylamine (NDMA) persistence within surface waters is a major concern for downstream communities exploiting these waters as drinking water supplies. The objective of this study is to develop a novel and efficient analytical method for NDMA via different technologies: pulsed splitless gas chromatography–nitrogen phosphorus detector (GC–NPD), large volume injection (LVI) gas chromatography–mass spectrometry (GC/MS) via programmable temperature vaporizer (PTV) inlet or PTV-gas chromatography– triple quadruple mass spectrometry (GC-MS/MS) and continuous liquid–liquid extraction. It was found that the sensitivity required for NDMA analysis by GC–NPD can only be achieved when the NPD bead is extremely clean. LVI via PTV can greatly improve GC-MS system sensitivity for analyzing NDMA. With the help of DB-624 (25 m × 200 μm × 1.12 μm) connected with DB-5MS (30 m × 250 μm × 0.25 μm) in series, PTV–GC/MS could overcome the matrix interference for the trace analysis of NDMA. Variable instrument conditions were studied in detail, with the optimized process being validated via precision and accuracy studies. PTV- triple quadruple GC-MS/MS system could efficiently remove the interference on a single DB-5MS (30 m × 250 μm × 0.25 μm) column with good sensitivity and selectivity. The developed methods have been successfully applied to test NDMA in different types of water samples with satisfactory results.


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