A plant essential oil gradient extraction device

An extraction device and a technology for plant essential oils, which are applied in the directions of essential oils/spices, fat production, etc., can solve the problems of increasing product costs, need to recover solvents, and consume solvents, and achieve the effects of reducing operating costs, rational use of energy, and high energy efficiency.

Active Publication Date: 2011-12-28
新疆天然芳香农业科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using organic solvent extraction to extract plant essential oils not only consumes solvent, but also the extraction solvent may bring impurities into the product, and also requires equipment for solvent recovery. The device is relatively complicated, which increases the cost of the product
Carbon dioxide supercritical extraction method, the extraction effect is good, but the equipment and operating costs are high
More importantly, the increase in temperature on the hot side will cause a substantial increase in the

Method used

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  • A plant essential oil gradient extraction device
  • A plant essential oil gradient extraction device
  • A plant essential oil gradient extraction device

Examples

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Effect test

Embodiment 1

[0039] Embodiment 1: extract peppermint essential oil and hydrosol with device of the present invention, device such as figure 1 , image 3 , Figure 4 As shown, it includes a closeable evaporator 1 with a raw material bed 2 inside. The top of the evaporator is connected to the inlet of a two-stage air pump 3, and the outlet of the air pump is connected to the cold side of the semiconductor refrigeration device. The semiconductor refrigeration device consists of three stages of semiconductor refrigeration. The refrigerators 4 (each refrigerator is a first-stage refrigeration unit) are connected in series, and the flow direction of the cold-side flow is sequentially from the first stage to the third stage. At the cold-side flow inlet of the first-stage to second-stage semiconductor refrigerators, there is a return flow jumper 5 with a valve, which is connected to the hot-side flow inlet of the current-stage semiconductor refrigerator. The outlet of the cold side of the final ...

Embodiment 2

[0041] Embodiment 2: extract peppermint essential oil and pure dew device as embodiment 1, there are 3 stages of semiconductor refrigeration units, at the 1st stage and the 2nd stage semiconductor refrigeration unit hot side outlets, respectively establish inter-stage condensate tank 15 ( See Image 6 ). There are return pipelines with valves from the bottom of the product collection tank to the second-stage condensate tank, and from the bottom of the second-stage condensate tank to the first-stage condensate tank. And the heights of the product collection tank, the second-stage condensate tank, and the first-stage condensate tank are 1.8 meters, 1.0 meters, and 0.2 meters in order, so that the condensate in the three tanks can have sufficient potential difference to flow back step by step , improve the clarity of product cutting, in addition in one or more condensate tanks, add fractionation tower section 15 (see Figure 7 ), the reflux flows in from the top of the tower se...

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Abstract

The invention provides a plant essence gradient extraction device, which comprises an evaporator with a built-in raw material bed layer, an exhaust pump, a gas condensing device, a circulating gas heating device and a product collecting tank, wherein the gas condensing device and the circulating gas heating device are formed by coupling a semiconductor cooling device; the cold side of the semiconductor cooling device serves as a gas condensing device and the hot side of the semiconductor cooling device serves as a circulating gas heating device; and the semiconductor cooling device is formed by connecting N stages of semiconductor cooling units in series; return crossing lines with valves are arranged at the cold side material outlet openings of the semiconductor cooling units from the 1st stage to the N-1th stage and are connected to the hot side material outlet openings of the semiconductor cooling units to regulate the temperature difference between the cold sides and the hot sidesof the semiconductor cooling units. Based on the requirements of the gradient extraction of the distillates of the plant essence, the device can provide cold energy and heat energy according to the required cooling and heating temperature, so that the device has high energy efficiency, is reasonable in energy utilization and low in cost.

Description

technical field [0001] The invention relates to a device for extracting active ingredients from plants. Specifically, it uses gas heating, condensation and circulation to extract plant essential oil in stages. Background technique [0002] Plant essential oils, also known as aromatic oils and volatile oils, are important natural spices. In the extraction of plant essential oils, the methods commonly used include distillation, extraction, pressing, leaching, adsorption, etc., among which steam distillation is the most common, and this method often produces components due to hydrolysis, thermal decomposition or other side reactions. Undesirable impurities or damage to effective components, and higher energy consumption. The extraction of plant essential oils by organic solvent extraction not only consumes solvent, but also the extraction solvent may bring impurities into the product. At the same time, equipment for solvent recovery is required, and the device is relatively c...

Claims

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Application Information

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IPC IPC(8): C11B9/00
Inventor 苏海任群英王力郭哲张鹏
Owner 新疆天然芳香农业科技有限公司
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