CN215404112U - Accurate extraction element of raw materials for preparation of acetic acid terpinyl ester - Google Patents

Abstract

The utility model discloses a raw material accurate extraction device for preparing acetic acid pine oil ester, which relates to the field of preparation of acetic acid pine oil raw materials, and provides the following scheme that the device comprises a heating device and a heat-insulating barrel, a first oil outlet pipe is communicated between the heating device and the heat-insulating barrel, a water pump is arranged on the first oil outlet pipe, the heating device is internally divided into a stirring chamber and a secondary heating chamber, the stirring chamber and the secondary heating chamber are provided with the same heating device, a motor is arranged in the heating device, the output end of the motor is fixedly provided with a stirring rod positioned in the stirring chamber, a driving rod is arranged in the secondary heating chamber, the driving rod and the stirring rod are both provided with belt pulleys, the driving rod is provided with a plurality of fan blades, a heating curved pipe and a water tank are arranged in the secondary heating chamber, and pine oil which cannot be directly used when being placed can be processed through the arrangement, so that the subsequent extraction can be effected without reheating.

Description

Accurate extraction element of raw materials for preparation of acetic acid terpinyl ester

Technical Field

The utility model relates to the field of preparation of acetic acid pine oil raw materials, in particular to a raw material accurate extraction device for preparing acetic acid pine oil ester.

Background

The terpinyl acetate is an esterification product of terpineol, has fresh and sweet fragrance, is similar to the smell of lemon and lavender, and has long fragrance retention time. The product is widely used for daily essences of lavender, spicy and citrus flavors and the like, and is also used for edible essences of white lemon, cherry, spicy and meat flavor and the like, plays a role in enhancing the spicy flavor in flavoring essential oil, and is a raw material for preparing bergamot oil, lavender oil, orange leaf oil and the like. The main raw material of the terpinyl acetate is turpentine.

Turpentine, one of essential oils, is an important industrial raw material. Turpentine is a liquid extracted from the resin of plants of the family Pinaceae by distillation or other methods, and contains terpene as the main component. Turpentine can be mixed with chloroform, ether or acetic acid at any ratio, but is insoluble in water. Turpentine oil belongs to flammable liquid with high flash point, has volatility and can generate a large amount of dense smoke during combustion. Turpentine oil is widely used as a chemical raw material, and has a chance to contact the turpentine oil in industries such as art glass, paint, camphor manufacturing, pharmacy, rosin manufacturing and the like. The existing turpentine is liquid extracted from turpentine of plant of Pinaceae by distillation or other method, and contains terpene as main ingredient. The volatile terpene mixed liquid with aromatic odor obtained by taking pine rich in rosin as a raw material through different processing modes is called turpentine. The components of turpentine oil are different according to the tree species, tree age and producing area, and the main components of the high-grade turpentine oil and the first-grade turpentine oil processed by the masson pine resin are a-pinene, and then b-pinene, limonene and the like. And also small amounts of sesquiterpenes, namely longifolene and caryophyllene. Turpentine is an excellent organic solvent and is widely used in the industries of paint, a thousand accelerator, an adhesive and the like. At present, the turpentine needs to be heated in the extraction process of a distillation method, but the traditional turpentine heating device has many problems in the heating distillation refining process, the traditional turpentine heating device can cause the turpentine in a heated cylinder to be heated unevenly, the evaporation of the turpentine is directly caused, namely, the distillation process is slow, the turpentine is not beneficial to efficient distillation refining of the turpentine, and sometimes, because of unstable factors appearing in processing, the heated turpentine needs to be placed for a while to be reused, but at the moment, the turpentine is slightly cooled, and if the turpentine is heated again, the turpentine is troublesome and laborious.

SUMMERY OF THE UTILITY MODEL

The utility model aims to solve the defects in the prior art and provides a raw material accurate extraction device for preparing terpinyl acetate.

In order to achieve the purpose, the utility model adopts the following technical scheme:

the utility model provides an accurate extraction element of raw materials for preparation of acetic acid pine oil ester, includes heating device and heat-preserving container, heating device with the intercommunication has first oil pipe between the heat-preserving container, first oil pipe is equipped with the water pump, divide into teeter chamber and secondary heating chamber in the heating device, the teeter chamber with the secondary heating chamber is equipped with same heating device, be equipped with the motor in the heating device, the output fixed mounting of motor has and is located puddler in the teeter chamber, be equipped with the actuating lever in the secondary heating chamber, the actuating lever with the puddler all is equipped with the belt pulley, be equipped with a plurality of flabellums on the actuating lever, be equipped with heating bent pipe and basin in the secondary heating chamber, heating bent pipe with be equipped with defeated oil pipe between the heat-preserving container.

Preferably, a water pump is arranged in the heat-preserving barrel, and the water outlet end of the water pump is communicated with the oil delivery pipe.

Preferably, the heating curved pipe penetrates through the secondary heating chamber and is communicated with the oil delivery pipe, and the oil delivery pipe and the water pump are both provided with valves.

Preferably, the heating curved pipe is positioned above the water tank.

Preferably, the water tank comprises a water delivery port, and the water delivery port is positioned on the front face of the heating device.

Preferably, an oil inlet pipe is arranged at the top of the heating device and communicated with the stirring chamber.

The utility model has the beneficial effects that:

1, the turpentine is input into the stirring chamber through the arrangement of the motor, the stirring rod, the stirring chamber and the first oil outlet pipe, the oil inlet pipe is started to drive the stirring rod to rotate, and the turpentine can be continuously stirred when the stirring rod rotates, so that the turpentine continuously rolls during heating, and the heating effect is better.

2, through the arrangement of the heat-insulating barrel, the secondary heating chamber, the heating curved pipe, the oil conveying pipe, the driving rod, the fan blades, the water tank, the belt pulley, the water conveying port, the first oil outlet pipe, the water pump and the heating device, when turpentine which is laid aside and can not be directly used is processed, the turpentine is stored in a heat-insulating manner through the heat-insulating barrel, then the turpentine is input into the secondary heating chamber through the heating curved pipe, water in the water tank is heated into steam, the steam is blown to the heating curved pipe through the fan blades, so that the hot steam is attached to the heating curved pipe, the turpentine is heated again, and the turpentine which is laid aside and can not be directly used can be processed through the arrangement, so that the turpentine which can not be directly used is not required to be heated again, and the effect of subsequent extraction can also be achieved.

Drawings

Fig. 1 is a schematic structural diagram of a raw material precision extraction device for terpinyl acetate preparation according to the present invention.

Fig. 2 is a schematic structural diagram of a front view cross section of a raw material precise extraction device for preparing terpinyl acetate according to the present invention.

Reference numbers in the figures: the device comprises a heating device 1, a heat-preserving barrel 2, an oil inlet pipe 3, a motor 4, a stirring rod 5, a stirring chamber 6, a secondary heating chamber 7, a heating curved pipe 8, an oil delivery pipe 9, a driving rod 10, fan blades 11, a water tank 12, a belt pulley 13, a water delivery port 14, a first oil outlet pipe 15, a water pump 16, a heating device 17 and a second oil outlet pipe 18.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments.

Referring to fig. 1-2, an accurate extraction element of raw materials for acetate pine oil ester preparation, including heating device 1 and heat-preserving container 2, it has first oil pipe 15 to communicate between heating device 1 and the heat-preserving container 2, first oil pipe 15 is equipped with water pump 16, divide into teeter chamber 6 and secondary heating chamber 7 in the heating device 1, teeter chamber 6 and secondary heating chamber 7 are equipped with same heating device 17, be equipped with motor 4 in the heating device 1, motor 4's output end fixed mounting has the puddler 5 that is located teeter chamber 6, be equipped with actuating lever 10 in the secondary heating chamber 7, actuating lever 10 and puddler 5 all are equipped with belt pulley 13, be equipped with a plurality of flabellums 11 on the actuating lever 10, be equipped with heating bent pipe 8 and basin 12 in the secondary heating chamber 7, be equipped with defeated oil pipe 9 between heating bent pipe 8 and the heat-preserving container 2.

A water pump 16 is arranged in the heat-preserving container 2, an oil delivery pipe 9 is communicated with the water outlet end of the water pump 16, a heating curved pipe 8 penetrates through a secondary heating chamber 7 and is communicated with the oil delivery pipe 9, the oil delivery pipe 9 and the water pump 16 are both provided with valves, the heating curved pipe 8 is positioned above a water tank 12, the water tank 12 comprises a water delivery port 14, the water delivery port 14 is positioned on the front face of the heating device 1, an oil inlet pipe 3 is arranged at the top of the heating device 1, and the oil inlet pipe 3 is communicated with the stirring chamber 6.

The working principle is as follows: when the utility model is used, turpentine is input into the stirring chamber 6, the stirring rod 5 is driven to rotate by starting the oil inlet pipe 3, the turpentine can be continuously stirred when the stirring rod 5 rotates, the heating device 17 is started to heat, so that the turpentine can be continuously rolled during heating, the heating effect is better, when the turpentine needs to be directly used, a valve of the second oil outlet pipe 18 is opened, the turpentine is discharged for use through the second oil outlet pipe 18, when the turpentine which is laid aside and can not be directly used is treated, the turpentine is stored in a heat preservation barrel 2 in a heat preservation manner, when the turpentine needs to be used, the water pump 16 is started to pump the turpentine in the heat preservation barrel 2, the turpentine is input into the heating curved pipe 8 through the oil pipeline 9 and is input into the secondary heating chamber 7, at the moment, water is input into the water tank 12, the heating device 17 is started to heat the water, high-heat water vapor is generated, the water in the water tank 12 is heated into vapor, at this moment, the stirring chamber 6 is operated continuously, the stirring rod 5 rotates to drive the driving rod 10 to rotate through the belt pulley 13, so that the fan blades 11 generate directional wind, water vapor is blown to the heating curved pipe 8 through the wind, and the hot water vapor is attached to the heating curved pipe 8, so that the turpentine is heated again, the turpentine which is placed and cannot be directly used can be treated through the arrangement, the turpentine does not need to be heated again, and the effect of subsequent extraction can be achieved.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", and the like, indicate orientations and positional relationships based on those shown in the drawings, and are used only for convenience of description and simplicity of description, and do not indicate or imply that the equipment or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be considered as limiting the present invention.

Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically defined otherwise.

The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and equivalent alternatives or modifications according to the technical solution of the present invention and the inventive concept thereof should be covered by the scope of the present invention.

Claims (6)

1. The utility model provides an accurate extraction element of raw materials for preparation of acetic acid pine oil ester, includes heating device (1) and heat-preserving container (2), its characterized in that, heating device (1) with intercommunication has first oil pipe (15) between heat-preserving container (2), first oil pipe (15) are equipped with water pump (16), divide into teeter chamber (6) and secondary heating chamber (7) in heating device (1), teeter chamber (6) with secondary heating chamber (7) are equipped with same heating device (17), be equipped with motor (4) in heating device (1), the output fixed mounting of motor (4) has and is located puddler (5) in teeter chamber (6), be equipped with actuating lever (10) in secondary heating chamber (7), actuating lever (10) with puddler (5) all are equipped with belt pulley (13), be equipped with a plurality of flabellum (11) on actuating lever (10), be equipped with heating bent pipe (8) and basin (12) in secondary heating room (7), heating bent pipe (8) with be equipped with defeated oil pipe (9) between heat-preserving container (2).

2. The device for accurately extracting the raw material for preparing the terpinyl acetate according to claim 1, characterized in that a water pump (16) is arranged in the heat-insulating barrel (2), and the water outlet end of the water pump (16) is communicated with the oil pipeline (9).

3. The device for accurately extracting the raw material for preparing terpinyl acetate according to claim 2, characterized in that the heating curved pipe (8) passes through the secondary heating chamber (7) and is communicated with the oil delivery pipe (9), and the oil delivery pipe (9) and the water pump (16) are provided with valves.

4. The apparatus for precisely extracting a raw material for terpinyl acetate preparation according to claim 1, wherein the heating curved pipe (8) is located above the water tank (12).

5. The apparatus for precisely extracting a raw material for terpinyl acetate preparation according to claim 4, wherein the water tank (12) comprises a water delivery port (14), and the water delivery port (14) is located at the front of the heating device (1).

6. The apparatus for precisely extracting raw material for terpinyl acetate preparation according to claim 4, wherein the top of the heating device (1) is provided with an oil inlet pipe (3), and the oil inlet pipe (3) is communicated with the stirring chamber (6).

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