Surface Modification of Metallic Reaction Vessels to Resist Scaling by Calcium Salts
Surface Modification of Metallic Reaction Vessels to Resist Scaling by Calcium Salts
批准号:
2386022
负责人:
金额:
$0.0万
依托单位:
依托单位国家:
英国
项目类别:
Studentship
财政年份:
2019
资助国家:
英国
项目状态:
已结题
起止时间:
2019 至 --
中文摘要
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英文摘要
Sugar cane ethanol plants use the addition of lime to the raw extracted juice in order to neutralise and clarify the juice. This leads to the juice becoming saturated with a range of calcium salts, notably sulphate, phosphate, silicate, and oxalate. This leads to the deposition of these salts as a hard scale on the insides of the tubes in the evaporators, where the sugar juice is concentrated by boiling off the water. The hard scale reduces the heat transfer rate in the evaporators, and would eventually lead to blockage of the tubes.Normal practice in Brazil is for the evaporators to be cleaned manually, as often as weekly. This involves personnel being lowered into the upper chamber of the evaporators and removing the scaling by "rodding", i.e. physical abrasion of the inner tube surfaces. Not only does this involve undesirable working in confined space, but it inevitably also leads to significant wear on the tubes leading to their frequent replacement. In countries where labour is most expensive, chemical cleaning has been attempted with rather mixed results. One difficulty is that such a diverse range of calcium salts is involved, a range of different (and mutually incompatible) chemical cleaners, including strong alkali, are needed to remove the deposits, so several cycles of cleaning are required each time, and some of the chemical cleaning agents also introduce additional hazards. Furthermore, each of the evaporator stages has a different combination of scalants, and requires different treatment.This project forms part of BP Group Research's response to this issue, and seeks to find means of treating the insides of evaporator tubes (and potentially other vulnerable surfaces) such that the calcium salts do not nucleate on those surfaces. It is understood that the evaporation of water must inevitably take the juice beyond the solubility limit of the salts concerned, so the aim must be to ensure that the salts either crystallise in the bulk rather than on the surface, or form solids which readily detach from the surface rather than form hard scales. In a practical implementation, this would require installation of filtration or settling equipment downstream of the evaporators to collect these calcareous precipitates.
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