Efficient fractionating tower for producing spice oil

Abstract

The utility model relates to the technical field of fractionating towers, in particular to a high-efficiency fractionating tower for producing spice oil. Comprising a bottom plate, a tower body and an auxiliary device, the auxiliary device comprises a heater, a first guide pipe, a condensation box, a second guide pipe, a condensation pipe, a receiving disc, an extraction assembly and a liquid guide assembly, during fractionation, raw materials are added into a storage cavity of the tower body through a feeding opening in the left side of the tower body, and then the heater works for heating to achieve fractionation; vapor with natural perfume oil is extracted and conveyed through the extraction assembly and the first guide pipe and is fed into the condensation pipe through the second guide pipe, when passing through the condensation pipe, the vapor can exchange heat with condensate circulating in the condensation box to achieve condensation and liquefaction, finally, condensed liquid falls into the receiving disc to be collected in a centralized mode, and therefore rapid condensation treatment after fractionation is achieved. Therefore, steam with natural perfume oil generated by fractionation can be condensed in time during fractionation production and processing of the perfume oil, the fractionation efficiency is improved, and efficient fractionation is realized.

Description

Technical Field

[0001] The utility model relates to the technical field of fractionation towers, in particular to a high-efficiency fractionation tower for producing spice oil. Background Art

[0002] When producing spice oil, a distillation tower will be used. The distillation towers currently on the market need to classify and store the distilled materials according to factors such as time and temperature. The operation is complicated, the effect is not good, and the distillation efficiency is low.

[0003] The prior art discloses a high-efficiency fractionation tower for producing spice oil, which comprises a tower body, a first fractionation plate, a second fractionation plate, a third fractionation plate, a discharge pipe, a heater and a controller. The fractionation tower is provided with the first fractionation plate, the second fractionation plate and the third fractionation plate, and the materials to be fractionated enter the tower body from the inlet. When the controller controls the operation of the heater at the bottom of the tower body, the materials with different boiling points fall on different fractionation plate layers and are discharged from the discharge pipe at the top of the tower body, and the fractionated materials are separated, thereby realizing one-time material processing, which is not only easy to operate but also has high fractionation efficiency.

[0004] However, when the above-mentioned distillation tower is actually used, the vapor containing natural flavor oil produced by the distillation cannot be condensed, which greatly reduces the distillation efficiency and is not conducive to efficient distillation. Utility Model Content

[0005] The utility model aims to provide a high-efficiency fractionation tower for the production of flavor oil, which aims to timely condense the vapor containing natural flavor oil produced by fractionation during the production and processing of flavor oil fractionation, thereby improving the fractionation efficiency and realizing high-efficiency fractionation.

[0006] To achieve the above-mentioned purpose, the utility model provides a high-efficiency fractionation tower for producing spice oil, comprising a bottom plate and a tower body, wherein the tower body is fixedly connected to the bottom plate and is located on the left side of the bottom plate, a feed port is arranged on the left side of the tower body, and an auxiliary device is also included;

[0007] The auxiliary device includes a heater, a first conduit, a condensation box, a second conduit, a condensation pipe, a receiving tray, an extraction assembly and a liquid guide assembly. The heater is fixedly connected to the tower body and is located at the bottom of the tower body. The first conduit is fixedly connected to the tower body and is located at the top of the tower body. The condensation box is fixedly connected to the bottom plate and is located on the right side of the bottom plate. The second conduit is fixedly connected to the condensation box and is located in the condensation box. The condensation pipe is detachably connected to the second conduit and the condensation box respectively, and is located on the side of the second conduit close to the condensation box. The receiving tray is arranged below the condensation box. The extraction assembly is arranged on the side of the first conduit close to the second conduit. The liquid guide assembly is arranged on both sides of the condensation box.

[0008] Wherein, the extraction component includes an extraction fan and a conveying pipe, the extraction fan is detachably connected to the first duct and is located on the side of the first duct away from the tower body; the conveying pipe is detachably connected to the extraction fan and the second duct respectively, and is located on the side of the extraction fan close to the second duct.

[0009] Wherein, the liquid guiding assembly comprises a liquid inlet seat and a liquid outlet seat, the liquid inlet seat is fixedly connected to the condensation box and is located on the left side of the condensation box; the liquid outlet seat is fixedly connected to the condensation box and is located on the right side of the condensation box.

[0010] Wherein, the auxiliary device further includes a temperature sensor, and the temperature sensor is fixedly connected to the liquid outlet seat and is located on the liquid outlet seat.

[0011] Wherein, the auxiliary device further comprises a fixed disk and a filter screen, wherein the fixed disk is fixedly connected to the liquid inlet seat and is located on the liquid inlet seat; the filter screen is fixedly connected to the fixed disk and is located on the fixed disk.

[0012] The utility model discloses a high-efficiency fractionation tower for producing spice oil, wherein the bottom plate is used for fixing the equipment, the tower body is installed on the left side of the bottom plate, a feeding port is arranged on the left side of the tower body, a switch door is arranged on the back, a heater is installed on the bottom of the tower body, a first conduit is installed on the top of the tower body, a condensation box is installed on the right side of the bottom plate, a second conduit is installed on one side of the condensation box, a condensation pipe is connected with the second conduit and the condensation box respectively, a receiving plate is arranged below the condensation box, an extraction component is arranged on one side of the first conduit close to the second conduit, a liquid guide component is arranged on both sides of the condensation box, and during fractionation, raw materials are added into the tower body storage cavity through the feeding port on the left side of the tower body, and then, the heater The steam containing natural flavor oil is extracted and transported through the extraction component and the first conduit, and is sent into the condenser through the second conduit. The liquid guide component introduces circulating condensate into the condenser box, so that the steam can exchange heat with the condensate when passing through the condenser to achieve condensation and liquefaction. Finally, the condensed liquid falls into the receiving plate for centralized collection, so as to achieve rapid condensation after fractionation, and further, when the flavor oil fractionation production and processing is carried out, the steam containing natural flavor oil produced by the fractionation can be condensed in time, which is beneficial to improve the fractionation efficiency and achieve efficient fractionation. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art are briefly introduced below.

[0014] Figure 1 It is a schematic diagram of the overall structure of a high-efficiency fractionating tower for producing spice oil according to the first embodiment of the utility model.

[0015] Figure 2 It is a front view of the condenser of the first embodiment of the utility model.

[0016] Figure 3 It is a schematic diagram of the overall structure of a high-efficiency fractionation tower for producing spice oil according to the second embodiment of the utility model.

[0017] Figure 4 It is a structural schematic diagram of a fixed disk according to the second embodiment of the utility model.

[0018] In the figure: 101-bottom plate, 102-tower body, 103-feeding port, 104-heater, 105-first conduit, 106-condensation box, 107-second conduit, 108-condensation pipe, 109-receiving plate, 110-extraction fan, 111-delivery pipe, 112-liquid inlet seat, 113-liquid outlet seat, 114-temperature sensor, 201-fixed plate, 202-filter screen. DETAILED DESCRIPTION

[0019] Embodiments of the present invention are described in detail below, and examples of the embodiments are shown in the accompanying drawings. The embodiments described below with reference to the accompanying drawings are exemplary and are intended to be used to explain the present invention, but should not be understood as limiting the present invention.

[0020] Embodiment 1:

[0021] like Figure 1 and Figure 2 As shown, Figure 1 This is a schematic diagram of the overall structure of a high-efficiency fractionation tower for the production of spice oil. Figure 2 It is a front view of the condenser 108. The utility model provides a high-efficiency fractionation tower for the production of flavor oil: comprising a bottom plate 101, a tower body 102 and an auxiliary device, wherein the auxiliary device comprises a heater 104, a first conduit 105, a condensation box 106, a second conduit 107, a condenser 108, a receiving plate 109, a temperature sensor 114, an extraction component and a liquid guide component, wherein the extraction component comprises an extraction fan 110 and a delivery pipe 111, and the liquid guide component comprises a liquid inlet seat 112 and a liquid outlet seat 113. The above scheme can realize that when the fractionation production and processing of flavor oil is carried out, the vapor with natural flavor oil produced by the fractionation can be condensed in time, which is beneficial to improve the fractionation efficiency and realize high-efficiency fractionation. It can be understood that the above scheme can improve the fractionation efficiency and realize high-efficiency fractionation.

[0022] In this embodiment, the tower body 102 is fixedly connected to the base plate 101 and is located on the left side of the base plate 101. A feeding port 103 is arranged on the left side of the tower body 102. The supporting feet of the tower body 102 are installed on the base plate 101 by bolts. The base plate 101 is used for fixed installation of equipment. A feeding port 103 is arranged on the left side of the tower body 102. The end of the round tube of the feeding port 103 is sealed by a threaded sealing cover to prevent impurities from entering the interior. A switch door is arranged on the back of the tower body 102 for easy closing and opening for internal cleaning. The equipment electric control box is arranged on the back side of the base plate 101. A discharge valve is arranged at the bottom of the back of the tower body 102 close to the heater 104. When opened, it is used for material discharge and does not interfere with the heater 104 when opened.

[0023] Among them, the heater 104 is fixedly connected to the tower body 102 and is located at the bottom of the tower body 102, the first conduit 105 is fixedly connected to the tower body 102 and is located at the top of the tower body 102, the condensation box 106 is fixedly connected to the bottom plate 101 and is located on the right side of the bottom plate 101, the second conduit 107 is fixedly connected to the condensation box 106 and is located in the condensation box 106, the condensation pipe 108 is detachably connected to the second conduit 107 and the condensation box 106 respectively, and is located on the side of the second conduit 107 close to the condensation box 106, the receiving plate 109 is arranged below the condensation box 106, the extraction component is arranged on the side of the first conduit 105 close to the second conduit 107, and the liquid guide component is arranged on both sides of the condensation box 106. The heater 104 is mounted at the bottom of the tower body 102 by bolts, the input side flange of the first conduit 105 is mounted at the top outlet of the tower body 102 by bolts, the back L-shaped mounting bracket of the condensation box 106 is connected to the bottom plate 101 by bolts to achieve fixation, the front side of the condensation box 106 is a detachable cover plate, the top flange of the second conduit 107 is threaded and detachable, and a skeleton-type sealing ring is arranged on the circular pipe section in contact with the condensation box 106 for sealing, and is fixed by bolts, the top connecting flange of the condensation pipe 108 is connected to the outlet side flange of the second conduit 107 by a screw nut, and the bottom connecting flange is connected to the condensation box 106 by bolts, the receiving plate 109 can be directly placed on the bottom plate 101, and is located below the condensation box 106, and is located below the output port of the condensation pipe 108, the extraction component is arranged on the side of the first conduit 105 close to the second conduit 107, and is used for steam extraction and transportation, and the liquid guide components are arranged on both sides of the condensation box 106, and are used for circulating and transporting condensate into the condensation box 106.

[0024] Secondly, the extraction fan 110 is detachably connected to the first duct 105 and is located at the side of the first duct 105 away from the tower body 102; the delivery pipe 111 is detachably connected to the extraction fan 110 and the second duct 107, respectively, and is located at the side of the extraction fan 110 close to the second duct 107. The inlet side flange of the extraction fan 110 is connected to the outlet side flange of the first duct 105 through a screw nut, the inlet side flange of the delivery pipe 111 is connected to the outlet side flange of the extraction fan 110 through a screw nut, and its outlet side flange is connected to the inlet side flange of the second duct 107 through bolts.

[0025] Then, the liquid inlet seat 112 is fixedly connected to the condensation tank 106 and is located on the left side of the condensation tank 106; the liquid outlet seat 113 is fixedly connected to the condensation tank 106 and is located on the right side of the condensation tank 106. The outlet side flange of the liquid inlet seat 112 is installed on the condensation tank 106 by bolts, and its inlet side flange is connected to the external condensate delivery pipeline. The inlet side flange of the liquid outlet seat 113 is installed on the condensation tank 106 by bolts, and the outlet side flange is connected to the external condensate recovery pipeline.

[0026] Finally, the temperature sensor 114 is fixedly connected to the liquid outlet seat 113 and is located on the liquid outlet seat 113. The temperature sensor 114 is installed on the liquid outlet seat 113 by bolts and is used to monitor the temperature of the condensate after heat exchange.

[0027] When using the utility model to carry out the fractionation production and processing of flavor oil, the steam with natural flavor oil produced by the fractionation can be condensed in time, which is beneficial to improve the fractionation efficiency. When realizing efficient fractionation, during fractionation, raw materials are added into the storage chamber of the tower body 102 through the feeding port 103 on the left side of the tower body 102, and then the heater 104 is controlled to work to heat and increase the temperature to realize fractionation. The steam with natural flavor oil is extracted and transported by the extraction fan 110, the conveying pipe 111 and the first conduit 105, and is sent into the storage chamber through the second conduit 107. In the condenser 108, at the same time, the liquid inlet seat 112 and the liquid outlet seat 113 cooperate to pass the circulating condensate into the condenser box 106, so that the steam can exchange heat with the condensate when passing through the condenser 108 to achieve condensation and liquefaction. Finally, the condensed liquid falls into the receiving plate 109 for centralized collection, thereby achieving rapid condensation treatment after distillation, and further achieving timely condensation treatment of the steam containing natural flavor oil produced by the distillation during the production and processing of flavor oil distillation, which is beneficial to improving the distillation efficiency and achieving efficient distillation.

[0028] Embodiment 2:

[0029] like Figure 3 and Figure 4 As shown, Figure 3 This is a schematic diagram of the overall structure of a high-efficiency fractionation tower for the production of spice oil. Figure 4 201 is a schematic diagram of the structure of a fixed disk 201. On the basis of the first embodiment, the utility model provides a high-efficiency fractionation tower for producing spice oil. The auxiliary device further includes a fixed disk 201 and a filter screen 202.

[0030] Among them, the fixed plate 201 is fixedly connected to the liquid inlet seat 112 and is located on the liquid inlet seat 112; the filter screen 202 is fixedly connected to the fixed plate 201 and is located on the fixed plate 201, the fixed plate 201 is installed at the entrance of the liquid inlet seat 112 by bolts, and the filter screen 202 is a perforated steel wire mesh, which is fixed to the fixed plate 201 by bolts.

[0031] In this embodiment, by providing the fixed disk 201 and the filter net 202, the condensate entering the condensation box 106 can be filtered to avoid internal blockage after long-term use.

[0032] What is disclosed above is only one or more preferred embodiments of the present application, and cannot be used to limit the scope of rights of the present application. Ordinary technicians in this field can understand that all or part of the processes of implementing the above embodiments and equivalent changes made according to the claims of the present application are still within the scope covered by the present application.

Claims

1. An efficient fractionation tower for producing spice oil, comprising a bottom plate and a tower body, wherein the tower body is fixedly connected to the bottom plate and is located on the left side of the bottom plate, and a feed port is arranged on the left side of the tower body, characterized in that: Also includes auxiliary devices; The auxiliary device includes a heater, a first conduit, a condensation box, a second conduit, a condensation pipe, a receiving tray, an extraction assembly and a liquid guide assembly. The heater is fixedly connected to the tower body and is located at the bottom of the tower body. The first conduit is fixedly connected to the tower body and is located at the top of the tower body. The condensation box is fixedly connected to the bottom plate and is located on the right side of the bottom plate. The second conduit is fixedly connected to the condensation box and is located in the condensation box. The condensation pipe is detachably connected to the second conduit and the condensation box respectively, and is located on the side of the second conduit close to the condensation box. The receiving tray is arranged below the condensation box. The extraction assembly is arranged on the side of the first conduit close to the second conduit. The liquid guide assembly is arranged on both sides of the condensation box.

2. The efficient fractionating tower for producing spice oil according to claim 1, characterized in that: The extraction assembly includes an extraction fan and a delivery pipe. The extraction fan is detachably connected to the first duct and is located on a side of the first duct away from the tower body. The delivery pipe is detachably connected to the extraction fan and the second duct respectively and is located on a side of the extraction fan close to the second duct.

3. The efficient fractionating tower for producing spice oil according to claim 1, characterized in that: The liquid guiding assembly comprises a liquid inlet seat and a liquid outlet seat, wherein the liquid inlet seat is fixedly connected to the condensation box and is located on the left side of the condensation box; the liquid outlet seat is fixedly connected to the condensation box and is located on the right side of the condensation box.

4. The efficient fractionating tower for producing spice oil as claimed in claim 3, characterized in that: The auxiliary device also includes a temperature sensor, which is fixedly connected to the liquid outlet seat and is located on the liquid outlet seat.

5. The efficient fractionating tower for producing spice oil as claimed in claim 3, characterized in that: The auxiliary device also includes a fixed disk and a filter screen. The fixed disk is fixedly connected to the liquid inlet seat and is located on the liquid inlet seat; the filter screen is fixedly connected to the fixed disk and is located on the fixed disk.

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