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Fully continuous process for the production of cocoa butter and cocoa powder from 50 native cocoa butter

机译:从50%天然可可脂生产可可脂和可可粉的完全连续过程

摘要

The continuous process to recover cocoa butter and powder, from a cocoa mass, has an initial roasting stage for the cocoa means followed by shelling. The cocoa bean kernels are reduced to a fluid cocoa mass in a watery emulsion to be separated into three components in a centrifugal action under high-speed rotation. The unwanted matter is spun out and retained matter is separated to give a pure and flavoursome cocoa powder and butter. ADVANTAGE - Eliminates fatty acids which would affect the taste. In an example, 1000 kg of finely chopped cocoa mass is produced from roasted and shelled Ghana cocoa beans, with well fermented kernels, and held in a V2A stainless steel vessel with a capacity of 7500 litres with a mass temp. of 65 deg.C for 15 mins., together with 5000 litres of water heated to 75 deg.C fed in over 15 mins. After filling, the matter is converted into an emulsion by a turbo mixer operating at 3000 rpm for 10 mins, and then passed to a V2A stainless steel tank with a slow paddle agitator rotating at 60 rpm. The emulsion is withdrawn continuously from the tank, within 30 mins., into a horizontal centrifuge operating at 32000 rpm with continuous take-off of thick matter. The cocoa butter which rises to the upper layer is separated and taken off to be pumped into an intermediate tank. The second layer thickness contains water with dissolved matter such as theobromine, the water soluble tannic matter and lower fatty acids and other substances with unpleasant smells. Additionally other substances are washed out such as soluble carbohydrates, pentoses, pentosane, xylane, galactans, araban etc. The thick matter portion, taken off continuously, is dried in a V2A double roller stainless steel vacuum dryer at a temp. of 75 deg.C to give a residual moisture content of 2.9%. The precipitated fine flake powder, with a pleasant light caramel-smelling character, is recovered at the rate of 41.2.8 kg with a residual fat content of 3.1%. The cocoa butter, in a recovered volume of 546.5 kg, is given a further rapid centrifuge spinning in the intermediate store vessel, to extract any small amts. of water for safety, and then chilled into blocks.
机译:从可可块中回收可可脂和粉末的连续过程具有可可装置的初始烘烤阶段,然后脱壳。可可豆仁在水乳状液中被还原成液体可可块,并在高速旋转下以离心作用分离为三个成分。多余的物质被甩出,残留的物质被分离出来,得到纯净可口的可可粉和黄油。优势-消除会影响口味的脂肪酸。在一个示例中,从加壳的加纳可可豆经过烘烤和去壳后,将其充分发酵,制成1000公斤切碎的可可块,并置于质量温度为7500升的V2A不锈钢容器中。将65摄氏度的水加热15分钟,并在15分钟内加入5000升加热到75摄氏度的水。填充后,物质通过涡轮混合器以3000 rpm的转速运转10分钟而转变为乳化液,然后通过缓慢的桨式搅拌器进入60 rpm的V2A不锈钢罐中。在30分钟内,将乳液从储罐中连续抽出到卧式离心机中,该离心机以32000 rpm的速度连续排出浓稠物质。分离出上升到上层的可可脂并取出,泵入中间罐。第二层厚度包含具有可溶物质的水,例如可可碱,水溶性单宁物质和低级脂肪酸以及其他具有难闻气味的物质。另外,其他物质也要洗掉,例如可溶性碳水化合物,戊糖,戊烷,二甲苯,半乳聚糖,阿拉伯树酯等。连续取出的稠物质部分在V2A双辊不锈钢真空干燥机中于一定温度下干燥。 75℃下的残余水分为2.9%。以41.2.8 kg的比例回收沉淀出的细薄片状粉末,具有令人愉悦的焦糖味特征,残留脂肪含量为3.1%。将回收量为546.5千克的可可脂在中间存储容器中进行进一步的快速离心纺丝,以提取任何小的安特。为了安全起见,然后将其冷冻成块。

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