Fractional separation device for petal essence solvent

Abstract

The invention provides a petal essence solvent fractionation device, and belongs to the technical field of plant essence extraction. Comprising a body, a feeding assembly is arranged at the top of the body, a cutting assembly is arranged at the bottom of the feeding assembly, the cutting assembly and the feeding assembly are fixedly connected through a valve, a distillation assembly is arranged at the bottom of the cutting assembly, the distillation assembly and the cutting assembly are fixedly connected through a valve, and an impurity removal assembly is arranged on one side of the distillation assembly. The impurity removal assembly comprises a sealing disc, a cooling assembly is fixedly connected to the bottom of the sealing disc, and an extraction assembly is arranged at the bottom of the cooling assembly. By arranging the extraction assembly, the petal essence is extracted in a graded mode so as to meet the differential requirements of diversified application scenes, meanwhile, due to the design of the two-way annular pipe, essence solvent steam and extract liquor steam can be liquefied at the same time, the solvent consumption cost is reduced, and meanwhile the resource circulation efficiency is improved.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of plant essence extraction, in particular to a petal essence solvent fractional separation device. BACKGROUND

[0002] The core function of petal essence is derived from the natural flavonoids, polyphenols, vitamins, amino acids, essential oils, polysaccharides and other active ingredients contained in the petals. These ingredients act on the skin after solvent extraction, and have skin care functions and mild experience. The active substances in the petals are mostly "lipid-soluble" or "difficult to dissolve in water" components, which cannot be fully extracted by water alone. The primary role of the solvent is to separate and dissolve the active ingredients in the petals from the cells to form a uniform purified liquid system, avoiding component precipitation or layering. At the same time, during the preparation of the essence, the solvent can quickly penetrate the petal tissue through soaking, distillation and other methods, maximizing the extraction of active ingredients (such as rose essential oil which requires ethanol or oil solvent extraction, and flavonoids in chrysanthemum which require alcohol solvent dissolution), reducing the waste of active ingredients.

[0003] The current mainstream extraction method in the industry is still based on traditional cooking method. This process usually requires preliminary extraction of active ingredients through high-temperature cooking, followed by fractional purification of the mixed extract to meet the different requirements of essence purity and active strength in different scenarios such as basic skin care, high-end cosmetics, and medicinal health care. However, this process has many significant defects: first, during the high-temperature cooking process, some heat-sensitive active ingredients (such as polyphenols and some vitamins) are prone to degradation, resulting in a significant reduction in the efficacy of the essence; second, the fractional extraction steps are complicated, requiring multiple transfers, filtrations, and purifications, which not only lengthens the process and reduces production efficiency, but also increases the risk of component contamination; third, the solvent recovery rate is low, and a large amount of solvent is easily lost during cooking and fractionalization, which not only increases production costs but also may cause environmental burden; fourth, the traditional process has limited effectiveness in targeted separation of different active ingredients, making it difficult to achieve precise fractionation, resulting in mixing of some high-value components with impurities, affecting product quality and application scenario adaptability.

[0004] Therefore, the present application provides a petal essence solvent fractional separation device to meet the needs. SUMMARY

[0005] The technical problem to be solved by the present application is to provide a petal essence solvent fractional separation device to solve the problem of the current cooking method extraction method, which has complicated fractional extraction steps, long process, low production efficiency, and increased risk of component contamination.

[0006] To solve the above technical problems, the present application provides the following technical solutions: The petal essence solvent fractional separation device, including the body, the body top is equipped with the feeding assembly, the feeding assembly bottom is equipped with the cutting assembly, the cutting assembly is connected with the feeding assembly through the valve, the cutting assembly bottom is equipped with the distillation assembly, the distillation assembly is connected with the cutting assembly through the valve, the distillation assembly one side is equipped with the impurity removal assembly; The impurity removal assembly includes a sealing disc, the bottom of the sealing disc is fixedly connected with a cooling assembly, and the bottom of the cooling assembly is provided with an extraction assembly.

[0007] Optionally, the cooling assembly includes a cooling barrel, an air inlet one is fixedly inserted into the inner wall of the top of the side of the distillation assembly, the air inlet one is fixedly connected with a steam pipe one at one end close to the distillation assembly, the air inlet one is fixedly connected with an annular pipe one at one end away from the distillation assembly, the annular pipe one is fixedly installed with a liquid outlet one at the bottom, a water inlet is fixedly inserted into the inner wall of the top of the cooling barrel, a drain is fixedly inserted into the inner wall of one side of the bottom of the cooling barrel, an exhaust outlet two is fixedly inserted into the inner wall of the bottom of the cooling barrel, the exhaust outlet two is fixedly connected with an air inlet two at the top, the air inlet two is located outside the cooling barrel, the air inlet two is fixedly connected with an annular pipe two at one end of the top, the annular pipe two is located inside the cooling barrel, the annular pipe two is fixedly connected with a liquid outlet two at the other end, and the liquid outlet two is fixedly inserted into the inner wall of the cooling barrel.

[0008] Optionally, the extraction assembly includes an extraction barrel, the extraction barrel is provided with three groups, and the three groups of extraction barrels are distributed in an array, the extraction barrel is fixedly inserted with an extraction liquid port at one side of the top, the extraction barrel is fixedly inserted with a solvent pipe at the front end of the top, the solvent pipe is provided with a cross pipe one at the other end, the cross pipe one is fixedly connected with the solvent pipe through a valve, the cross pipe one is fixedly connected with the liquid outlet one at one end of the top, the extraction barrel is fixedly inserted with a steam pipe two at the end of the top, the steam pipe two is provided with a cross pipe two at the other end, the cross pipe two is fixedly connected with the steam pipe two through a valve, the cross pipe two is fixedly connected with the exhaust outlet two at one end of the top, the extraction barrel is fixedly inserted with a collection pipe at the bottom of the front end, and the extraction barrel is fixedly inserted with a negative pressure pipe at the top of the end.

[0009] Optionally, the sealing disc is fixedly installed with a connecting cover at the top, the sealing disc is fixedly inserted with a connecting pipe at the bottom, the connecting pipe is fixedly inserted with the air inlet one at the side wall of the bottom, the sealing disc is fixedly installed with a dust removal pipe at the top, the dust removal pipe is fixedly connected with the connecting pipe at the bottom, a silica gel disc is fixedly installed in the inner wall of the dust removal pipe close to the top, the dust removal pipe is fixedly inserted with an air inlet pipe at the middle position of one side close to the distillation assembly, and the dust removal pipe is fixedly inserted with an air suction pipe at the middle position of the other side.

[0010] Optionally, the connecting pipe is internally provided with an electrode rod, the electrode rod is movably inserted with the dust removal pipe, the top of the electrode rod is fixedly connected with a connecting plate, the top of the connecting plate is fixedly connected with a supporting disc, the top of the supporting disc is fixedly installed with a generator, the top of the generator is provided with a motor cover, the bottom of the motor cover is fixedly connected with the supporting disc, the top of the supporting disc is fixedly installed with an electric push rod at both ends, the top of the electric push rod is provided with a protective cover, the top of the electric push rod is fixedly connected with the inner wall of the protective cover, and the bottom of the protective cover is fixedly connected with the top of the connecting cover.

[0011] Optionally, the distillation assembly comprises a distillation barrel, a waste port is formed in the bottom of one side of the distillation barrel, and an exhaust port one is fixedly installed at the top of the side close to the cooling assembly.

[0012] Optionally, the cutting assembly comprises a cutting barrel, the cutting barrel is fixedly installed with a connecting ring at the top, the connecting ring is fixedly installed with a conical cover at the center position, and the conical cover is fixedly installed with a servo motor two on the inner wall.

[0013] Optionally, the sleeve is fixedly sleeved at the output end of the servo motor two, the cutter seat is fixedly installed on the outer wall of the sleeve, the cutter blade is fixedly installed on one side of the cutter seat, and the cutter array is fixedly installed on the inner wall of the cutting barrel.

[0014] Optionally, the feeding assembly comprises a storage barrel, the storage barrel is fixedly connected with a sealing cover at the top, and the sealing cover is movably inserted with a feeding port at the top of one side.

[0015] Optionally, the servo motor one is movably inserted and fixed at the top center position of the sealing cover, the stirring rod is fixedly installed at the output end of the servo motor one, the motor cover is arranged at the top of the servo motor one, and the bottom of the motor cover is fixedly connected with the top of the sealing cover.

[0016] Compared with the prior art, the present application has at least the following advantages: In the above scheme, by arranging the extraction assembly and the cooling assembly, flexible operation can be realized according to different purity requirements, the petal essence can be extracted in stages, the differentiated requirements of diversified application scenes (such as basic skin care and high-end makeup) can be met, the cooling assembly with a double-path annular pipe design can quickly liquefy the essence solvent vapor generated during distillation on one hand, so as to ensure that active ingredients (such as flavonoids, polyphenols and essential oils) remain stable in a low-temperature environment and avoid high-temperature degradation; on the other hand, the extraction liquid vapor evaporated during the extraction process can be recovered synchronously, and after being liquefied by cooling, the extraction liquid vapor can be reused, so that the solvent consumption cost is reduced and the resource recycling efficiency is improved.

[0017] By setting the impurity removal assembly, the static electric field generated by the electrode rod precisely adsorbs the tiny impurities and other pollutants in the essence solvent, thereby improving the purity of the essence from the source. After the extraction is completed, the electric push rod drives the electrode rod to move upwards, the silica gel disc automatically wipes the impurities adsorbed on the surface of the electrode rod, and the impurities are quickly discharged by cooperating with the air suction pipe connected with the air blower. Cleaning can be completed without disassembling the equipment, avoiding the problem of filter blockage caused by impurity accumulation, ensuring the continuity of the production process. At the same time, the sealing design of the sealing disc and the connecting cover effectively isolates the cooling water from the impurity removal unit, preventing secondary pollution and further improving the safety and purity of the essence product.

[0018] By setting the cutting assembly and the feeding assembly, the servo motor drives the stirring rod to uniformly mix the petal raw material and the solvent, and simultaneously performs preheating treatment. This not only accelerates the penetration speed of the solvent into the petal tissue, but also provides a temperature basis for the subsequent distillation process, greatly shortening the distillation time. The cutting assembly refines the pretreated raw material into tiny particles, increases the contact area between the raw material and the solvent, and makes the active ingredients such as flavonoids and essential oils more easily extracted, avoiding the problem that the internal components of the raw material are difficult to release in the traditional cooking method, significantly improving the utilization rate of the raw material and reducing resource waste. BRIEF DESCRIPTION OF DRAWINGS

[0019] The accompanying drawings, which are incorporated herein and constitute part of the specification, illustrate embodiments of the application and, together with the description, further serve to explain the principles of the application and to enable a person skilled in the relevant art to implement and use the application.

[0020] Figure 1 It is a whole structure schematic diagram of the petal essence solvent fractional separation device; Figure 2 It is a structure schematic diagram of the feeding assembly, cutting assembly and distillation assembly of the petal essence solvent fractional separation device; Figure 3 It is a sectional split structure schematic diagram of the cutting assembly, distillation assembly and feeding assembly of the petal essence solvent fractional separation device; Figure 4 It is a sectional split structure schematic diagram of the cutting assembly of the petal essence solvent fractional separation device; Figure 5 It is a sectional split structure schematic diagram of the distillation assembly of the petal essence solvent fractional separation device; Figure 6 It is a sectional structure schematic diagram of the impurity removal assembly and the cooling assembly of the petal essence solvent fractional separation device; Figure 7 It is a sectional split structure schematic diagram of the cooling assembly of the petal essence solvent fractional separation device; Figure 8 It is a sectional split structure schematic diagram of the impurity removal assembly of the petal essence solvent fractional separation device; Figure 9 It isFigure 8 Local enlarged structure schematic diagram; Figure 10 For Figure 9 Local sectional split enlarged structure schematic diagram; Figure 11 For extraction assembly and cooling assembly sectional structure schematic diagram; Figure 12 For extraction assembly sectional split structure schematic diagram.

[0021] Reference signs: 100, body; 110, feeding assembly; 111, storage barrel; 112, sealing cover; 113, feeding port; 114, servo motor one; 115, stirring rod; 116, motor cover; 120, cutting assembly; 121, cutting barrel; 122, connecting ring; 123, conical cover; 124, servo motor two; 125, sleeve; 126, knife seat; 127, knife blade; 128, knife array; 130, distillation assembly; 131, distillation barrel; 132, waste port; 133, exhaust port one; 140, impurity removal assembly; 141, sealing disc; 142, connecting cover; 143, connecting pipe; 144, dust removal pipe; 145, silica gel disc; 146, air inlet pipe; 147, air suction pipe; 148, electrode rod; 149, connecting plate; 150, support disc; 151, generator; 152, motor cover; 153, electric push rod; 154, protective cover; 160, cooling assembly; 161, cooling barrel; 162, air inlet port one; 163, steam pipe one; 164, annular pipe one; 165, liquid discharge port one; 166, water inlet; 167, water discharge port; 168, exhaust port two; 169, air inlet port two; 170, annular pipe two; 171, liquid discharge port two; 180, extraction assembly; 181, extraction barrel; 182, extraction liquid port; 183, solvent pipe; 184, cross pipe one; 185, steam pipe two; 186, cross pipe two; 187, collection pipe; 188, negative pressure pipe.

[0022] As shown in the drawings, in order to clearly realize the structure of the embodiments of the present application, specific structures and devices are marked in the drawings, but this is only for the need of illustration, and is not intended to limit the present application in this specific structure, device and environment, and those skilled in the art can adjust or modify these devices and environment according to specific needs. DETAILED DESCRIPTION

[0023] The petal essence solvent fractional separation device provided by the present application is described in detail below in combination with the drawings and specific embodiments. It should be noted that the following embodiments are the best, preferred embodiments, and other alternative embodiments can also be used by those skilled in the art for implementation of some known technologies; and the drawings are only used to more specifically describe the embodiments, and are not intended to specifically limit the present application.

[0024] As Figures 1 to 12As shown, the embodiment of the application provides a petal essence solvent fractional separation device, which comprises a body 100, the top of the body 100 is provided with a feeding assembly 110, the bottom of the feeding assembly 110 is provided with a cutting assembly 120, the cutting assembly 120 is fixedly connected with the feeding assembly 110 through a valve, the bottom of the cutting assembly 120 is provided with a distillation assembly 130, the distillation assembly 130 is fixedly connected with the cutting assembly 120 through a valve, one side of the distillation assembly 130 is provided with an impurity removal assembly 140, the impurity removal assembly 140 comprises a sealing disc 141, the bottom of the sealing disc 141 is fixedly connected with a cooling assembly 160, the bottom of the cooling assembly 160 is provided with an extraction assembly 180, the cooling assembly 160 comprises a cooling barrel 161, the top inner wall of the cooling barrel 161 near one side of the distillation assembly 130 is fixedly inserted with an air inlet one 162, one end of the air inlet one 162 near the distillation assembly 130 is fixedly connected with a steam pipe one 163, one end of the air inlet one 162 away from the distillation assembly 130 is fixedly connected with an annular pipe one 164, the bottom of the annular pipe one 164 is fixedly installed with a liquid outlet one 165, the top end inner wall of the cooling barrel 161 is fixedly inserted with a water inlet 166, the bottom side inner wall of the cooling barrel 161 is fixedly inserted with a water outlet 167, the bottom inner wall of the cooling barrel 161 is fixedly inserted with an air outlet two 168, the top of the air outlet two 168 is fixedly connected with an air inlet two 169, the air inlet two 169 is located outside the cooling barrel 161, one end of the top of the air inlet two 169 is fixedly connected with an annular pipe two 170, the annular pipe two 170 is located inside the cooling barrel 161, the other end of the annular pipe two 170 is fixedly connected with a liquid outlet two 171, the liquid outlet two 171 is fixedly inserted with the inner wall of the cooling barrel 161, wherein the steam pipe one 163 can discharge the essence solvent vapor in the distillation assembly 130 into the air inlet one 162, then the cooling water conveyed through the water inlet 166 can liquefy the vapor into a liquid state, the water inlet 166 is connected with cooling water, then the liquid essence solvent flows to the liquid outlet one 165 through the annular pipe one 164, and then enters the bottom extraction assembly 180, the water outlet 167 is connected with a collection device, so as to facilitate the secondary utilization of the cooling water, the air outlet two 168 is used for collecting the extraction liquid evaporated in the extraction assembly 180, the extraction liquid vapor moves to the air inlet two 169 through the air outlet two 168, the air inlet two 169 is located outside the cooling barrel 161, so as to prevent the liquid from being liquefied in advance and then flowing back to the extraction assembly 180, the extraction liquid vapor moves to the annular pipe two 170 in the air inlet two 169, and then flows to the liquid outlet two 171 through the cooling water, the liquid outlet two 171 is connected with a collection device, which can collect the extraction liquid for secondary utilization.

[0025] As Figures 2 to 6As shown, the extraction assembly 180 includes three groups of extraction barrels 181 arranged in an array, the top side of the extraction barrel 181 is inserted and fixed with an extraction liquid port 182, the top front end of the extraction barrel 181 is inserted and fixed with a solvent pipe 183, the other end of the solvent pipe 183 is provided with a cross pipe one 184, the cross pipe one 184 is fixedly connected with the solvent pipe 183 through a valve, the top end of the cross pipe one 184 is fixedly connected with the bottom of the liquid outlet one 165, the top end of the extraction barrel 181 is inserted and fixed with a steam pipe two 185, the other end of the steam pipe two 185 is provided with a cross pipe two 186, the cross pipe two 186 is fixedly connected with the steam pipe two 185 through a valve, the top end of the cross pipe two 186 is fixedly connected with the exhaust port two 168, the front end of the bottom of the extraction barrel 181 is inserted and fixed with a collection pipe 187, the end of the top of the extraction barrel 181 is inserted and fixed with a negative pressure pipe 188, wherein the extraction barrel 181 is provided with three groups, which can be used according to the required different purity of essence liquid, the left and right two bottoms of the cross pipe one 184 and the cross pipe two 186 are provided with valves, when different extraction barrels 181 are used, the corresponding valve can be opened, the essence solvent cooled in the upper cooling assembly 160 flows into the corresponding extraction barrel 181, then the extraction liquid of the corresponding purity is added, the essence solvent is extracted and processed into essence liquid, the negative pressure pipe 188 is externally connected with a negative pressure motor, which can extract the pressure in the extraction barrel 181, so that the solvent part of the extraction liquid and the essence solvent is quickly evaporated, then the essence liquid is left, the collection pipe 187 is externally connected with a collection device, which can collect the essence liquid extracted in the extraction barrel 181, the extraction barrel 181 is provided with a heating wire, which can heat the extraction barrel 181 to accelerate the evaporation extraction process.

[0026] As Figures 2 to 6As shown, the top of the sealing disc 141 is fixedly provided with a connecting cover 142, the bottom of the sealing disc 141 is fixedly provided with a connecting pipe 143, the bottom of the connecting pipe 143 is fixedly provided with a sidewall of the air inlet one 162, the top of the sealing disc 141 is fixedly provided with a dust removal pipe 144, the bottom of the dust removal pipe 144 is fixedly connected with the top of the connecting pipe 143, a silica gel disc 145 is fixedly installed on the inner wall of the dust removal pipe 144 close to the top, an air inlet pipe 146 is fixedly inserted into the dust removal pipe 144 close to the middle of one side of the distillation assembly 130, an air suction pipe 147 is fixedly inserted into the dust removal pipe 144 close to the middle of the other side, an electrode rod 148 is arranged in the connecting pipe 143, the electrode rod 148 is movably inserted into the dust removal pipe 144, the top of the electrode rod 148 is fixedly connected with a connecting plate 149, the top of the connecting plate 149 is fixedly connected with a supporting disc 150, the top of the supporting disc 150 is fixedly provided with a generator 151, the top of the generator 151 is provided with a motor cover 152, the bottom of the motor cover 152 is fixedly connected with the supporting disc 150, the top of the supporting disc 150 is fixedly provided with an electric push rod 153, the top of the electric push rod 153 is provided with a protective cover 154, the top of the electric push rod 153 is fixedly connected with the inner wall of the protective cover 154, the bottom of the protective cover 154 is fixedly connected with the top of the connecting cover 142, wherein the impurity removal assembly 140 and the cooling assembly 160 are separated by the sealing disc 141 to prevent the cooling water from entering the impurity removal assembly 140, the water inlet 166 is higher than the air inlet one 162 and the air inlet two 169 in height, so that the essence solvent in the air inlet one 162 is in a liquid-gas coexistence state, then the generator 151 generates electricity for the electrode rod 148, so that the electrode rod 148 generates an electrostatic field to adsorb the impurities in the essence solvent, when the extraction of the essence solvent is completed, the generator 151 stops working, the electric push rod 153 works to drive the supporting disc 150 to move upward, so that the silica gel disc 145 wipes off the impurities adsorbed on the bottom of the electrode rod 148, the diameters of the holes in the top and the bottom of the dust removal pipe 144 are greater than the diameter of the top of the electrode rod 148, so as to facilitate the movement of the electrode rod 148, the diameter of the hole in the silica gel disc 145 is smaller than the diameter of the bottom of the electrode rod 148, so as to facilitate the wiping of the impurities on the electrode rod 148 when the electrode rod 148 moves upward, the air suction pipe 147 is connected with a fan, when the impurities on the electrode rod 148 fall off, the fan works to suck away the impurities falling off from the electrode rod 148 in the dust removal pipe 144.

[0027] As Figures 2 to 6As shown, the distillation assembly 130 includes a distillation barrel 131, a waste port 132 is formed in the bottom of one side of the distillation barrel 131, an exhaust port one 133 is fixedly installed on the top of the side of the distillation barrel 131 close to the cooling assembly 160, the exhaust port one 133 is fixedly connected with one end of the steam pipe one 163, the cutting assembly 120 includes a cutting barrel 121, the cutting barrel 121 is fixedly installed with a connecting ring 122 on the top, the connecting ring 122 is fixedly installed with a conical cover 123 at the center position, the conical cover 123 is fixedly installed with a servo motor two 124 on the inner wall, the servo motor two 124 is fixedly sleeved with a sleeve 125 at the output end, the sleeve 125 is fixedly installed with a knife seat 126 on the outer wall, the knife seat 126 is fixedly installed with a blade 127 on one side, the cutting barrel 121 is fixedly installed with a knife array 128 on the inner wall, the feeding assembly 110 includes a storage barrel 111, the storage barrel 111 is fixedly connected with a sealing cover 112 on the top, the sealing cover 112 is fixedly inserted with an inlet port 113 on one side of the top, the sealing cover 112 is fixedly inserted with a servo motor one 114 at the center position of the top, the servo motor one 114 is fixedly installed with a stirring rod 115 at the output end, the servo motor one 114 is provided with a motor cover 116 on the top, and the motor cover 116 is fixedly connected with the sealing cover 112 on the bottom, wherein the waste port 132 is used for collecting waste after distillation in the distillation barrel 131, the exhaust port one 133 can exhaust the distilled essence solvent gas in the distillation barrel 131 into the steam pipe one 163, and then move into the air inlet one 162, the distillation barrel 131 is provided with heating wires inside, which can heat and distill the raw materials in the distillation barrel 131, the connecting ring 122 is used for supporting and fixing the conical cover 123, the conical cover 123 is used for supporting and fixing the servo motor two 124, the servo motor two 124 can drive the sleeve 125 to rotate, so that the knife seat 126 drives the blade 127 to rotate, and then cooperates with the knife array 128 to cut the raw materials, so that the cut raw materials can be quickly distilled in the distillation barrel 131, the waste of raw materials can be reduced, and the cutting assembly 120 is fixedly provided with a valve at the bottom, which can prevent the essence solvent gas in the distillation barrel 131 from being exhausted into the cutting assembly 120, the storage barrel 111 is provided with heating wires inside, which can preheat the raw materials and the solvent, thereby improving the working efficiency of the bottom distillation assembly 130, the inlet port 113 is used for placing raw materials and distillation solvents, the servo motor one 114 can drive the stirring rod 115 to rotate, thereby stirring the raw materials and the solvent in the storage barrel 111, accelerating the preheating of the raw materials, and the valve at the bottom of the feeding assembly 110 can prevent the raw materials in the storage barrel 111 from being preheated and then entering the cutting assembly 120.

[0028] The technical scheme provided by the application has the following working principles: When the petal essence solvent needs to be fractionated, the corresponding extraction barrel 181 can be used for different purity essences, then the valves of cross pipe one 184 and cross pipe two 186 corresponding to the extraction barrel 181 are opened, then the raw materials and the distillation solvent are placed in the storage barrel 111 through the feed port 113, then the servo motor one 114 works to stir the raw materials and the solvent, at the same time the storage barrel 111 preheats the raw materials, after preheating, the valve is opened, the raw materials with mixed solvent in the feeding assembly 110 fall into the cutting assembly 120, then the servo motor two 124 works to drive the sleeve 125 to make the knife seat 126 drive the knife blade 127 to rotate, then cooperate with the knife array 128 to cut the raw materials, then the cut raw materials fall into the distillation barrel 131 in the distillation assembly 130, thereby improving the utilization rate of raw materials and reducing resource waste, after all the raw materials are cut, the valve at the bottom of the cutting assembly 120 is closed, the distillation barrel 131 heats the raw materials with mixed solvent to evaporate the essence into gas, then enters the vapor pipe one 163 through the exhaust port one 133, finally enters the gas inlet one 162, then the water inlet 166 transports cooling water in the cooling barrel 161, so that the vapor in the gas inlet one 162 is liquefied, at the same time the generator 151 works to generate electricity for the electrode rod 148, so that the electrode rod 148 generates an electrostatic field to adsorb impurities in the essence solvent, then the essence solvent flows to the annular pipe one 164 through the gas inlet one 162, then flows to the liquid outlet one 165, finally flows to the corresponding extraction barrel 181 through the cross pipe one 184, then pours into the extraction liquid required by the corresponding purity through the extraction liquid port 182, then the extraction barrel 181 is subjected to negative pressure treatment through the negative pressure pipe 188, then the extraction barrel 181 is heated, so that the extraction liquid and the essence solvent evaporate, thereby leaving the essence liquid, the evaporated extraction liquid and solvent are discharged to the cross pipe two 186 through the vapor pipe two 185, then discharged to the annular pipe two 170 through the exhaust port two 168 and the gas inlet two 169, finally cooled by the cooling water in the cooling barrel 161, then discharged through the liquid outlet two 171, so as to be used twice later, thereby reducing the solvent consumption cost and improving the resource recycling efficiency, after extraction, the essence liquid in the extraction barrel 181 is collected through the collection pipe 187, at the same time the generator 151 stops working, the electric push rod 153 works to drive the support disc 150 to move upward, so that the silica gel disc 145 wipes off the impurities adsorbed at the bottom of the electrode rod 148, then the fan works to suck the impurities falling from the electrode rod 148 in the dust removal pipe 144, thereby improving the safety and purity of the essence product.

[0029] The present application encompasses any alternatives, modifications, equivalent methods and solutions made to the essence and scope of the present application. In order to make the public have a thorough understanding of the present application, specific details are described in the following preferred embodiments of the present application, and the present application can also be fully understood without the description of these details to those skilled in the art. In addition, in order to avoid unnecessary confusion to the essence of the present application, well-known methods, processes, procedures, elements and circuits, etc. are not described in detail.

[0030] The above is only the preferred embodiment of the present application, and it should be pointed out that for ordinary skilled in the art, without departing from the principles of the present application, a number of improvements and refinements can also be made, which should be considered as the protection scope of the present application.

Claims

1. A petal essence solvent fractionation and separation device, characterized in that, The device includes a body (100), a feeding assembly (110) on the top of the body (100), a cutting assembly (120) at the bottom of the feeding assembly (110), the cutting assembly (120) and the feeding assembly (110) being fixedly connected by a valve, a distillation assembly (130) at the bottom of the cutting assembly (120), the distillation assembly (130) and the cutting assembly (120) being fixedly connected by a valve, and a purification assembly (140) on one side of the distillation assembly (130). The impurity removal component (140) includes a sealing disk (141), and a cooling component (160) is fixedly connected to the bottom of the sealing disk (141). An extraction component (180) is provided at the bottom of the cooling component (160).

2. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, The cooling assembly (160) includes a cooling tank (161). An air inlet (162) is fixedly inserted into the inner top wall of the cooling tank (161) near the distillation assembly (130). A steam pipe (163) is fixedly connected to the end of the air inlet (162) near the distillation assembly (130), and an annular pipe (164) is fixedly connected to the end of the air inlet (162) away from the distillation assembly (130). A drain outlet (165) is fixedly installed at the bottom of the annular pipe (164). A water inlet (166) is fixedly inserted into the inner wall of the top end of the cooling tank (161). A drain outlet (167) is fixedly inserted into the inner wall of one side of the bottom. An exhaust outlet (168) is fixedly inserted into the inner wall of the bottom of the cooling tank (161). An air inlet (169) is fixedly connected to the top of the exhaust outlet (168). The air inlet (169) is located outside the cooling tank (161). An annular pipe (170) is fixedly connected to one end of the top of the air inlet (169). The annular pipe (170) is located inside the cooling tank (161). A drain outlet (171) is fixedly connected to the other end of the annular pipe (170). The drain outlet (171) is inserted and fixed into the inner wall of the cooling tank (161).

3. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, The extraction assembly (180) includes an extraction tank (181), which has three sets arranged in an array. An extraction liquid port (182) is inserted and fixed to one side of the top of the extraction tank (181), and a solvent tube (183) is inserted and fixed to the front end of the top of the extraction tank (181). A cross tube (184) is provided at the other end of the solvent tube (183), and the cross tube (184) is fixedly connected to the solvent tube (183) by a valve. One end of the top of the cross tube (184) is connected to the drain port. The bottom of the extraction tank (181) is fixedly connected to the extraction tank (181). A steam pipe (185) is inserted and fixed at the top end of the extraction tank (181). A cross pipe (186) is provided at the other end of the steam pipe (185). The cross pipe (186) and the steam pipe (185) are fixedly connected by a valve. One end of the top of the cross pipe (186) is fixedly connected to the exhaust port (168). A collection pipe (187) is inserted and fixed at the bottom of the front end of the extraction tank (181). A negative pressure pipe (188) is inserted and fixed at the top of the end of the extraction tank (181).

4. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, A connecting cover (142) is fixedly installed on the top of the sealing disc (141), and a connecting pipe (143) is fixedly inserted into the bottom of the sealing disc (141). The bottom of the connecting pipe (143) is fixedly inserted into the side wall of the air inlet (162). A dust removal pipe (144) is fixedly installed on the top of the sealing disc (141). The bottom of the dust removal pipe (144) is fixedly connected to the top of the connecting pipe (143). A silicone disc (145) is fixedly installed on the inner wall of the dust removal pipe (144) near the top. An air inlet pipe (146) is fixedly inserted into the middle of the side of the dust removal pipe (144) near the distillation assembly (130). An air suction pipe (147) is fixedly inserted into the middle of the other side of the dust removal pipe (144).

5. The petal essence solvent fractionation and separation device according to claim 4, characterized in that, The connecting pipe (143) is provided with an electrode rod (148) inside. The electrode rod (148) is movably connected to the dust removal pipe (144). A connecting plate (149) is fixedly connected to the top of the electrode rod (148). A support plate (150) is fixedly connected to the top of the connecting plate (149). A generator (151) is fixedly installed on the top of the support plate (150). A motor cover (152) is provided on the top of the generator (151). The bottom of the motor cover (152) is fixedly connected to the support plate (150). Electric push rods (153) are fixedly installed at both ends of the top of the support plate (150). A protective cover (154) is provided on the top of the electric push rod (153). The top of the electric push rod (153) is fixedly connected to the inner wall of the protective cover (154). The bottom of the protective cover (154) is fixedly connected to the top of the connecting cover (142).

6. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, The distillation assembly (130) includes a distillation tank (131), a waste outlet (132) is provided at the bottom of one side of the distillation tank (131), and an exhaust port (133) is fixedly installed on the top of the side of the distillation tank (131) near the cooling assembly (160), and the exhaust port (133) is fixedly connected to one end of a steam pipe (163).

7. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, The cutting assembly (120) includes a cutting barrel (121), a connecting ring (122) is fixedly installed on the top of the cutting barrel (121), a conical cover (123) is fixedly installed at the center of the connecting ring (122), and a servo motor (124) is fixedly installed on the inner wall of the conical cover (123).

8. The petal essence solvent fractionation and separation device according to claim 7, characterized in that, The output end of the servo motor (124) is fitted with a sleeve (125), a tool holder (126) is fixedly installed on the outer wall of the sleeve (125), a blade (127) is fixedly installed on one side of the tool holder (126), and a blade array (128) is fixedly installed on the inner wall of the cutting barrel (121).

9. The petal essence solvent fractionation and separation device according to claim 1, characterized in that, The feeding assembly (110) includes a storage bin (111), a sealing cap (112) is fixedly connected to the top of the storage bin (111), and a feed inlet (113) is inserted and fixed to one side of the sealing cap (112).

10. The petal essence solvent fractionation and separation device according to claim 9, characterized in that, A servo motor (114) is inserted and fixed at the center of the top of the sealing cover (112). A stirring rod (115) is fixedly installed at the output end of the servo motor (114). A motor cover (116) is provided on the top of the servo motor (114). The bottom of the motor cover (116) is fixed to the top of the sealing cover (112).

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