Biodiesel oil preparing process and apparatus

A preparation process and biodiesel technology, which are applied in the biodiesel preparation process and the field of devices thereof, can solve the problems of reducing the contact of reactant molecules, high energy consumption in the distillation process, and high requirements on oil quality, and achieve the improvement of reaction speed and reduction of finished product color and luster. , the effect of short distillation time

Inactive Publication Date: 2007-08-22
JIANGXI XINSHIDAI OIL & FAT IND
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  • Abstract
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Problems solved by technology

The weak point of its existence of above-mentioned two kinds of processing methods is, the first, above-mentioned two kinds of production methods are independent equipment design is various, general acid-catalyzed esterification reaction is applicable to acidified oil, quality-saving oil, waste oil etc.; And Alkaline catalyzed transesterification requires relatively low acid value and high requirements for oil quality. Second, the conventional esterification process is a reaction between liquid phase and liquid phase. Oil is a liquid phase, and methanol is also a liquid phase. In the presence of a catalyst, molecular motion and mechanical stirring are used to promote the collision

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  • Biodiesel oil preparing process and apparatus
  • Biodiesel oil preparing process and apparatus
  • Biodiesel oil preparing process and apparatus

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Embodiment Construction

[0019] Specific implementation plan

[0020] The process principle of the invention adopts the methanol vapor phase to enter the oil phase from the bottom by bubbling, and with the aid of mechanical stirring, the oil molecules and the methanol molecules are fully contacted and combined, which greatly accelerates the reaction speed.

[0021] The process includes the esterification reaction, adding methanol, concentrated sulfuric acid and raw oil into the stirred reactor 1 and heating to carry out the esterification reaction. The process flow is shown in Figure 2. The said esterification reaction is supplemented by entering or refluxing. The methanol entering the reactor 1 is heated by the methanol steam generator 2 to become methanol vapor, and then enters the reactor 1 from the bottom of the reactor 1 through the valve 7.

[0022] The process equipment is shown in Figure 2, including a stirred reactor 1, a methanol recovery device 6, a qualified methanol receiver 4, a methanol pum...

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Abstract

The present invention relates to biodiesel oil preparing process and apparatus. In the heated esterification reaction of methanol, concentrated sulfuric acid and material oil inside a stirring reactor, the methanol is first heated and gasified into methanol vapor before entering the reactor from the bottom, and this results in liquid phase-gas phase reaction with high reaction speed and short reaction period. Therefore, the present invention has the features of fast reaction speed, short reaction period, saving in material, lowered heat energy consumption and other advantages, and is suitable for preparing biodiesel oil with different kinds of material oil.

Description

Technical field [0001] The invention relates to a biodiesel preparation process and its device, in particular to a methanol vapor phase system and reflux process and its device in the esterification reaction of a biodiesel preparation process, and a methyl ester vapor phase continuous distillation process and its device. Background technique [0002] At present, biodiesel is mainly produced by chemical methods, that is, animal and vegetable oils and methanol are transesterified under acid-base catalyst and high temperature to generate corresponding fatty acid methyl esters, which are then washed and dried to obtain biodiesel. The conventional production process of acid-catalyzed esterification reaction is raw material pretreatment, removing impurities and dehydration in the raw oil, esterification reaction, separation, distillation, alcohol recovery and purification treatment, and its esterification reaction, adding methanol and Concentrated sulfuric acid and raw oil are heated t...

Claims

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Application Information

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IPC IPC(8): C10G3/00
CPCY02E50/13Y02E50/10Y02P30/20
Inventor 陆寿全
Owner JIANGXI XINSHIDAI OIL & FAT IND
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