CN112915568A - Medicinal soybean oil rectifying equipment - Google Patents
Medicinal soybean oil rectifying equipment Download PDFInfo
- Publication number
- CN112915568A CN112915568A CN202110357926.6A CN202110357926A CN112915568A CN 112915568 A CN112915568 A CN 112915568A CN 202110357926 A CN202110357926 A CN 202110357926A CN 112915568 A CN112915568 A CN 112915568A
- Authority
- CN
- China
- Prior art keywords
- self
- homogeneous
- counterweight
- rectification
- homogeneous mixing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
Abstract
The invention discloses medicinal soybean oil rectifying equipment which comprises a multilayer inverted triangular vortex type step-by-step homogeneous rectifying part, a multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower, a self-counterweight type rectifying foam-trapping part, a tower plate and a self-telescopic homogeneous mixing component, wherein the self-telescopic homogeneous mixing component is connected with the lower end of the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower, the tower plate is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower, the multilayer inverted triangular vortex type homogeneous step-by-step rectifying part is arranged on the tower plate, the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying part is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower, and the self-counterweight type foam-trapping part is detachably arranged at the upper end of the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower. The invention belongs to the technical field of medicinal soybean oil rectifying towers, and particularly relates to medicinal soybean oil rectifying equipment.
Description
Technical Field
The invention belongs to the technical field of medicinal soybean oil rectifying towers, and particularly relates to medicinal soybean oil rectifying equipment.
Background
The quality index of the medicinal soybean oil is extremely high, in the production of the medicinal soybean oil, the decolored clean soybean oil is rectified by a rectifying tower, and volatile impurity components in the soybean oil are separated in the rectifying process of the soybean oil, so that the quality index reaches the requirement. In the prior art, no rectifying tower suitable for the production of medicinal soybean oil exists, a negative pressure rectifying tower for material rectification is generally provided with a tower body, the lower part of the tower body is provided with a tower kettle, the tower kettle is provided with a discharge hole and a heating device, the upper part of the tower body is provided with a feed inlet and a vacuum interface, the middle part in the tower body is provided with a tower plate, a foam catcher is arranged in the tower body and between the tower plate and the vacuum interface, and the rectifying tower can also be provided with no tower plate for the more volatile impurity components in the rectified material. When the tower is used, materials are added from a feed inlet at the upper part of the tower body, the materials flow down to a certain height in the tower kettle through the tower plate, the materials in the tower kettle are heated by the heating device, volatile components in the materials volatilize, the volatile components are further separated from the materials after the tower plate rises, the materials are sucked out by vacuum, and the materials from which the volatile components are separated in the tower kettle flow out through a discharge outlet of the tower kettle. The negative pressure stripping rectifying tower has only one section, and is suitable for separating volatile impurity component with volatility in certain limited range, and the volatile impurity component outside the limited range may not be separated.
The medicinal soybean oil three-section rectifying tower of patent No. 200910013118.7, there is consecutive upper, middle, lower three-section tower, there is the baffle between the three-section tower, the lower part of every section tower is the tower cauldron, there is direct steam inlet tower cauldron lateral wall, middle, there is the column plate at the middle part in the lower section tower body, there is the mist eliminator column top, the tower body lateral wall of mist eliminator top has the vacuum interface, on, there is the U-shaped pipe heater in the lower section tower cauldron, lower section tower cauldron lateral wall has the discharge gate, upper segment upper portion lateral wall has the feed inlet, even there is the air duct upper portion of upper segment tower and the mist eliminator below of middle section tower, there is the baffling board in the middle section tower cauldron, even there is the cluster link between the column plate, the cluster link cover between the adjacent column plate has the. The tower body is divided into an upper section, a middle section and a lower section, so that materials are rectified in three sections, the process conditions of the three-section rectification are adjusted to adapt to the separation of volatile impurity components with different volatility, and the volatile impurity components with larger volatility range in the materials can be separated. The parts in the tower can be disassembled and are easy to clean, but the rectification cannot be more precise.
Disclosure of Invention
In order to solve the existing problems, the invention provides medicinal soybean oil rectification equipment, a self-telescopic homogeneous mixing component is used for quickly freezing dropwise rectification liquid entering a cooling part in a quick-cooling mode, the dropwise rectification liquid and raw liquid to be mixed are arranged in a self-telescopic homogeneous mixing elastic part, pressure is applied to the self-telescopic homogeneous mixing elastic part through the volume of the mixed raw liquid, the self-telescopic homogeneous mixing elastic part is elastically deformed, extrusion force is applied to mixed liquid in the self-telescopic homogeneous mixing elastic part, the homogeneous mixed liquid quickly impacts into a multilayer inverted triangular eddy current type homogeneous self-counterweight stepwise rectification tower under the pushing of the extrusion force to form local eddy, meanwhile, the multilayer inverted triangular eddy current type stepwise homogeneous rectification part takes a triangle with a wide bottom and a narrow top as a flow channel, the homogeneous mixed liquid is further promoted to form local counterweight eddy current to increase the probability of separating volatile matters, a counterweight type polymerization tank and an arc-shaped counterweight block are arranged on the autologous rectification foam catching part and are matched with each other, the medicinal soybean oil with the upper end to be separated from the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower is stirred and polymerized again, and the rectifying effect is further realized.
The technical scheme adopted by the invention is as follows: the invention relates to medicinal soybean oil rectifying equipment which comprises a multilayer inverted triangle vortex type step-by-step homogeneous rectifying part, a multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower, a self-counterweight type rectifying foam catching part, a tower plate and a self-telescopic homogeneous mixing component, wherein the self-telescopic homogeneous mixing component is connected with the lower end of the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower, the self-telescopic homogeneous mixing component is used for mixing a raw liquid to be rectified and a dropwise rectifying liquid and then conveying the mixed liquid into the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower, the tower plate is arranged in the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower, the multilayer inverted triangle vortex type step-by-step homogeneous rectifying part is arranged on the tower plate, the multilayer inverted triangle type homogeneous rectifying part is arranged in the multilayer inverted triangle type homogeneous self-counterweight step-by-step rectifying tower, the self-counterweight type rectification foam catching piece is detachably arranged at the upper end of the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectification tower; the self-telescopic homogeneous mixing assembly comprises a homogeneous mixing elastic part fixing seat, a self-telescopic homogeneous mixing elastic part and a cooling part, the self-telescopic homogeneous mixing elastic part is arranged on the homogeneous mixing elastic part fixing seat, the homogeneous mixing elastic part fixing seat plays a role in supporting and fixing the self-telescopic homogeneous mixing elastic part, the cooling part is connected with the self-telescopic homogeneous mixing elastic part, dropwise rectification liquid is quickly frozen into dropwise ice through the cooling part and enters the self-telescopic homogeneous mixing elastic part, and meanwhile, raw liquid needing rectification enters the self-telescopic homogeneous mixing elastic part to form homogeneous mixed liquid; the self-telescopic homogeneous mixing elastic part comprises a homogeneous mixing outlet, a first limiting part, a self-telescopic homogeneous mixing rigid shell, a homogeneous mixing inlet, a second limiting part and a self-telescopic homogeneous mixing elastic inner layer, the self-telescopic homogeneous mixing rigid shell is arranged on a homogeneous mixing elastic part fixing seat, the homogeneous mixing elastic part fixing seat is used for fixing the self-telescopic homogeneous mixing rigid shell, the homogeneous mixing outlet and the homogeneous mixing inlet are arranged on the self-telescopic homogeneous mixing rigid shell in a penetrating manner, the self-telescopic homogeneous mixing elastic inner layer is arranged in the self-telescopic homogeneous mixing rigid shell, the self-telescopic homogeneous mixing elastic inner layer is arranged on the homogeneous mixing outlet and the homogeneous mixing inlet, the first limiting part and the second limiting part are arranged in the self-telescopic homogeneous mixing elastic inner layer, and the first limiting part is arranged on the homogeneous mixing outlet, the limiting part II is arranged on the homogeneous mixing inlet, the cooling part is connected with the self-telescopic homogeneous mixing elastic inner layer through the homogeneous mixing inlet, the dropwise solid rectification liquid enters the self-telescopic homogeneous mixing elastic inner layer through the homogeneous mixing inlet, and the raw liquid to be rectified enters the self-telescopic homogeneous mixing elastic inner layer through the homogeneous mixing inlet to form homogeneous mixed liquid; a plurality of groups of inverted triangular vortex type through holes are uniformly arranged in the multilayer inverted triangular vortex type step-by-step homogeneous rectification piece at equal intervals; the homogeneous mixed liquid is taken as a flow channel through a plurality of groups of multilayer inverted triangular vortex type through holes arranged in a trapezoidal structure with a wide bottom and a narrow top, so that the homogeneous mixed liquid is promoted to form a local vortex to increase the probability of separating volatile matters; the self-counterweight type rectification foam catching part is arranged in an arc shape, the self-counterweight type rectification foam catching part is provided with a counterweight type polymerization groove, an arc-shaped counterweight block and a self-counterweight type rectification foam catching mesh hole, the self-counterweight type rectification foam catching mesh hole is in a trapezoidal arrangement with a narrow lower part and a wide upper part, the self-counterweight type rectification foam catching mesh hole is provided with a plurality of groups, the plurality of groups of self-counterweight type rectification foam catching mesh holes are uniformly arranged on the self-counterweight type rectification foam catching part at equal intervals, the counterweight type polymerization groove is arranged on the self-counterweight type rectification foam catching part and is close to the self-counterweight type rectification foam catching mesh hole, the counterweight type polymerization groove is provided with a plurality of groups, the counterweight type polymerization groove is arranged on the counterweight type rectification foam catching part at equal intervals, the arc-shaped counterweight block is arranged in the counterweight type polymerization groove and is close to the counterweight type rectification foam catching mesh hole, and the arc-shaped counterweight block is provided with, the arc-shaped balancing weight is matched with and arranged in the counterweight type polymerization tank, the self-counterweight type rectification foam catching piece reduces fog drops entrainment, local polymerization is formed through the counterweight type polymerization tank, homogeneous mixed liquid is separated through the arc-shaped balancing weight during polymerization, and the rectification effect is promoted in one-to-one integration.
Further, a multilayer inverted triangular vortex type step-by-step homogeneous rectification layer, a heating conduit, a steam outlet pipe and a return pipe are arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, the heating conduit is arranged at the lower end in the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower, the multilayer inverted triangular vortex type step-by-step homogeneous rectification layer is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, the multilayer inverted triangular vortex step-by-step homogeneous rectifying layer is provided with a plurality of groups, the plurality of groups of multilayer inverted triangular vortex step-by-step homogeneous rectifying layers are arranged in the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower at intervals, the multilayer inverted triangular vortex step-by-step homogeneous rectification piece is arranged in the multilayer inverted triangular vortex step-by-step homogeneous rectification layer, the steam outlet pipe and the return pipe are arranged at the upper end of the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower.
Further, homogeneous mixed liquor in the telescopic homogeneous mixed elastic inner layer enters the multilayer inverse triangular eddy current type homogeneous self-counterweight step-by-step rectifying tower through the homogeneous mixed outlet.
Furthermore, a first electromagnetic control valve is arranged in the homogeneous mixing discharge port, a second electromagnetic control valve is arranged in the homogeneous mixing inlet, the first electromagnetic control valve is opened after the telescopic homogeneous mixing elastic inner layer is continuously expanded under the pressure of the homogeneous mixing liquid, and the homogeneous mixing liquid in the telescopic homogeneous mixing elastic inner layer rapidly impacts the multi-layer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower under the extrusion of the telescopic homogeneous mixing elastic inner layer.
Further, the vertical section of the multilayer inverted triangular vortex step-by-step homogeneous rectification piece is in a trapezoidal arrangement.
Furthermore, a drop-shaped liquid inlet and a drop-shaped solid outlet are formed in the cooling piece, and the drop-shaped solid outlet is connected with the homogeneous mixing inlet.
The invention with the structure has the following beneficial effects: the invention provides medicinal soybean oil rectification equipment, wherein a self-telescopic homogeneous mixing component is used for quickly freezing dropwise rectification liquid entering a cooling part in a quick-cooling mode, the rectification liquid and stock solution to be mixed are arranged in a self-telescopic homogeneous mixing elastic part, pressure is applied to the self-telescopic homogeneous mixing elastic part through the self volume of the mixed stock solution, so that the self-telescopic homogeneous mixing elastic part is elastically deformed, extrusion force is applied to mixed liquid in the self-telescopic homogeneous mixing elastic part, the homogeneous mixed liquid is quickly impacted and enters a multilayer inverted triangular vortex homogeneous self-weight step-by-step rectification tower under the pushing of the extrusion force to form local vortex, the homogeneous mixed liquid is used as a circulation channel through a plurality of groups of multilayer inverted triangular vortex type through holes arranged in a trapezoid structure with wide lower part and narrow upper part, the homogeneous mixed liquid is promoted to form local vortex to increase the probability of separating volatile matters, a self-weight type rectification foam catching part is provided with a polymerization tank and an arc-shaped balancing weight block which are matched with each other, the medical soybean oil of the rectifying tower is formed into local polymerization through the counterweight polymerization tank at the same time, and the separation of homogeneous mixed liquid is carried out through the arc-shaped balancing weight during polymerization, so that the realization of the rectifying effect is promoted in one aggregation.
Drawings
FIG. 1 is a schematic structural diagram of a medicinal soybean oil rectification apparatus according to the present invention;
FIG. 2 is a front view of a self-retracting homomixer assembly of a medicinal soybean oil rectification apparatus of the present invention;
FIG. 3 is a front view of a multilayer inverted triangular vortex homogeneous self-counterweight progressive rectifying tower of the medicinal soybean oil rectifying device of the present invention;
FIG. 4 is a schematic structural diagram of an autologous counterweight type distillation foam-catching member of the medicinal soybean oil distillation equipment of the present invention;
FIG. 5 is a schematic structural diagram of a multi-layer inverted triangular vortex-type step-by-step homogeneous rectification piece of the medicinal soybean oil rectification device of the present invention;
FIG. 6 is a cross-sectional view of a multilayer inverted triangular vortex type step-by-step homogeneous rectification piece of a medicinal soybean oil rectification apparatus of the present invention;
FIG. 7 is a sectional view of an autocounterweight type distillation mist catching member of the medicinal soybean oil distillation device of the present invention;
wherein, 1, multilayer inverted triangle vortex type cascade homogeneous rectification parts, 2, multilayer inverted triangle vortex type homogeneous counterweight cascade rectification tower, 3, autologous counterweight type rectification foam catching parts, 4, tower plates, 5, self-telescopic homogeneous mixing components, 6, homogeneous mixing elastic part fixing seats, 7, self-telescopic homogeneous mixing elastic parts, 8, cooling parts, 9, homogeneous mixing discharge ports, 10, limiting parts I, 11, self-telescopic homogeneous mixing rigid shell, 12, homogeneous mixing inlet ports, 13, limiting parts II, 14, self-telescopic homogeneous mixing elastic inner layers, 15, multilayer inverted triangle vortex type through holes, 16, counterweight type polymerization tanks, 17, arc-shaped balancing weights, 18, autologous counterweight type rectification foam catching meshes, 19, multilayer inverted triangle vortex type cascade homogeneous rectification layers, 20, heating conduits, 21, steam outlet pipes, 22, return pipes, 23, electromagnetic control valves I, 24. a second electromagnetic control valve 25, a drop-shaped liquid inlet 26 and a drop-shaped solid outlet.
Detailed Description
The technical solutions of the present invention will be further described in detail with reference to specific implementations, and all the portions of the present invention not described in detail are the prior art.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance. The present invention will be described in further detail with reference to the accompanying drawings.
As shown in figures 1-7, the medicinal soybean oil rectifying device comprises a multilayer inverted triangle vortex type step-by-step homogeneous rectifying part 1, a multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower 2, a self-counterweight type rectifying foam catching part 3, a tower plate 4 and a self-telescopic homogeneous mixing component 5, wherein the self-telescopic homogeneous mixing component 5 is connected with the lower end of the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower 2, the self-telescopic homogeneous mixing component 5 is used for mixing a raw liquid to be rectified and a dropwise rectifying liquid and then conveying the mixed liquid into the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower 2, the tower plate 4 is arranged in the multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectifying tower 2, the multilayer inverted triangle type homogeneous rectifying part 1 is arranged on the tower plate 4, the multilayer inverted triangle vortex type homogeneous step-by-step rectifying part 1 is arranged in the multilayer inverted triangle type homogeneous self-counterweight step-by-step rectifying tower 2, the self-counterweight type rectification foam catching part 3 is detachably arranged at the upper end of a multilayer inverted triangle vortex type homogeneous self-counterweight step-by-step rectification tower 2, a self-telescopic homogeneous mixing component 5 is used for quickly freezing dropwise rectification liquid entering a cooling part 8 in a quick-cooling mode, the dropwise rectification liquid and raw liquid to be mixed are arranged in the self-telescopic homogeneous mixing component 5, pressure is applied to the self-telescopic homogeneous mixing component 5 through the self volume of the mixed raw liquid, so that the interior of the self-telescopic homogeneous mixing component 5 is elastically deformed, extrusion force is applied to mixed liquid in the self-telescopic homogeneous mixing component, the homogeneous mixed liquid is quickly impacted to enter the multilayer inverted triangle vortex type homogeneous counterweight step-by-step rectification tower 2 under the extrusion force to form a local vortex, and meanwhile, the multilayer inverted triangle vortex type homogeneous rectification part 1 takes a triangle with a wide bottom and a narrow top as a flow channel to further promote the homogeneous mixed liquid to form a local vortex, the arrangement of the self-counterweight type rectification foam catching piece 3 ensures that the medicinal soybean oil with the upper end about to separate from the multilayer inverted triangular vortex type homogeneous self-counterweight stepwise rectification tower 2 is stirred and polymerized again so as to further realize the rectification effect; the self-telescopic homogeneous mixing component 5 comprises a homogeneous mixing elastic part fixing seat 6, a self-telescopic homogeneous mixing elastic part 7 and a cooling part 8, the self-telescopic homogeneous mixing elastic part 7 is arranged on the homogeneous mixing elastic part fixing seat 6, the homogeneous mixing elastic part fixing seat 6 plays a role in supporting and fixing the self-telescopic homogeneous mixing elastic part 7, the cooling part 8 is connected with the self-telescopic homogeneous mixing elastic part 7, dropwise rectified liquid is quickly frozen into dropwise ice through the cooling part 8 and enters the self-telescopic homogeneous mixing elastic part 7, and meanwhile, raw liquid needing to be rectified enters the self-telescopic homogeneous mixing elastic part 7 to form homogeneous mixed liquid; the self-telescopic homogeneous mixing elastic part 7 comprises a homogeneous mixing outlet 9, a first limiting part 10, a self-telescopic homogeneous mixing rigid shell 11, a homogeneous mixing inlet 12, a second limiting part 13 and a self-telescopic homogeneous mixing elastic inner layer 14, the self-telescopic homogeneous mixing rigid shell 11 is arranged on a homogeneous mixing elastic part fixing seat 6, the homogeneous mixing elastic part fixing seat 6 is used for fixing the self-telescopic homogeneous mixing rigid shell 11, the homogeneous mixing outlet 9 and the homogeneous mixing inlet 12 are arranged on the self-telescopic homogeneous mixing rigid shell 11, the self-telescopic homogeneous mixing elastic inner layer 14 is arranged in the self-telescopic homogeneous mixing rigid shell 11, the self-telescopic homogeneous mixing elastic inner layer 14 is arranged on the homogeneous mixing outlet 9 and the homogeneous mixing inlet 12, the first limiting part 10 and the second limiting part 13 are arranged in the self-telescopic homogeneous mixing elastic inner layer 14, the first limiting part 10 is arranged on the homogeneous mixing outlet 9, the second limiting part 13 is arranged on the homogeneous mixing inlet 12, the cooling part 8 is connected with the self-telescopic homogeneous mixing elastic inner layer 14 through the homogeneous mixing inlet 12, the dropwise solid rectification liquid enters the self-telescopic homogeneous mixing elastic inner layer 14 through the homogeneous mixing inlet 12, the raw liquid to be rectified enters the self-telescopic homogeneous mixing elastic inner layer 14 through the homogeneous mixing inlet 12 to form homogeneous mixed liquid, the raw liquid gradually expands and expands from the telescopic homogeneous mixing elastic inner layer 14 as the raw liquid continuously enters the homogeneous mixed liquid, slides to the self-telescopic homogeneous mixing rigid shell 11 along the homogeneous mixing outlet 9 and the homogeneous mixing inlet 12, the first electromagnetic control valve 23 is arranged in the homogeneous mixing outlet 9, the second electromagnetic control valve 24 is arranged in the homogeneous mixing inlet 12, and the self-telescopic homogeneous mixing elastic inner layer 14 expands continuously under the pressure of the homogeneous mixed liquid, opening a first electromagnetic control valve 23, and rapidly impacting the homogeneous mixed liquid in the self-telescopic homogeneous mixed elastic inner layer 14 into the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower 2 under the extrusion of the self-telescopic homogeneous mixed elastic inner layer 14; multilayer inverted triangular vortex type through holes 15 are formed in the multilayer inverted triangular vortex type step-by-step homogeneous rectification piece 1, the multilayer inverted triangular vortex type through holes 15 are arranged in a trapezoidal structure with the width at the bottom and the width at the top, the multilayer inverted triangular vortex type through holes 15 are arranged in a plurality of groups, the multilayer inverted triangular vortex type through holes 15 in the plurality of groups are uniformly arranged in the multilayer inverted triangular vortex type step-by-step homogeneous rectification piece 1 at equal intervals, and the vertical section of the multilayer inverted triangular vortex type step-by-step homogeneous rectification piece 1 is arranged in a trapezoidal shape; the homogeneous mixed liquid is a circulation channel through a plurality of groups of multilayer inverted triangular vortex type through holes 15 arranged in a trapezoidal structure with the lower width and the upper width being narrow, so that the homogeneous mixed liquid is promoted to form a local vortex to increase the probability of separating volatile substances.
The self-counterweight type rectification foam catching member 3 is arranged in an arc shape, a counterweight type polymerization groove 16, an arc-shaped balancing weight 17 and a self-counterweight type rectification foam catching mesh 18 are arranged on the self-counterweight type rectification foam catching member 3, the self-counterweight type rectification foam catching mesh 18 is in a trapezoid shape with a narrow lower part and a wide upper part, a plurality of groups of self-counterweight type rectification foam catching meshes 18 are arranged on the self-counterweight type rectification foam catching member 3, a plurality of groups of self-counterweight type rectification foam catching mesh 18 are uniformly arranged on the self-counterweight type rectification foam catching member 3 at intervals, a counterweight type polymerization groove 16 is arranged on the self-counterweight type rectification foam catching member 3 and is close to the self-counterweight type rectification foam catching mesh 18, a plurality of groups of counterweight type polymerization grooves 16 are arranged on the self-counterweight type rectification foam catching member 3 at intervals, an arc-shaped balancing weight 17 is arranged in the counterweight type polymerization groove 16 and is close to the self-counterweight type rectification foam catching mesh 18, and a plurality of, a plurality of groups of arc-shaped balancing weights 17 are matched and arranged in the counterweight type polymerization tank 16, the self-counterweight type rectification foam catching piece 3 reduces entrainment, local polymerization is formed through the counterweight type polymerization tank 16, homogeneous mixed liquid is separated through the arc-shaped balancing weights 17 during polymerization, and the rectification effect is promoted to be realized in one-to-one integration.
Homogeneous mixed discharge port 9 is arranged on the side wall of multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2 and is close to the bottom wall of multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2, homogeneous mixed liquid in telescopic homogeneous mixed elastic inner layer 14 enters multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2 through homogeneous mixed discharge port 9, multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2 is internally provided with multilayer inverted triangle vortex homogeneous rectifying layer 19, heating conduit 20, steam outlet pipe 21 and return pipe 22, heating conduit 20 is arranged at the lower end in multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2, multilayer inverted triangle vortex homogeneous rectifying layer 19 is arranged in multilayer inverted triangle vortex homogeneous self-counterweight stepwise rectifying tower 2, multilayer inverted triangle vortex homogeneous rectifying layer 19 is provided with a plurality of groups, a plurality of groups of multilayer inverted triangle vortex homogeneous self-balancing rectifying layers 19 are arranged in the multilayer inverted triangle vortex homogeneous self-balancing stepwise rectifying tower 2 at intervals, multilayer inverted triangle vortex homogeneous rectifying parts 1 are arranged in the multilayer inverted triangle vortex homogeneous self-balancing stepwise rectifying layer 19, and a steam outlet pipe 21 and a return pipe 22 are arranged at the upper end of the multilayer inverted triangle vortex homogeneous self-balancing stepwise rectifying tower 2.
The cooling element 8 is provided with a drop-shaped liquid inlet 25 and a drop-shaped solid outlet 26, and the drop-shaped solid outlet 26 is connected with the homogeneous mixing inlet 12.
When the self-expanding homogeneous mixed liquid distillation tower is used, dropwise solid rectification liquid enters the self-expanding homogeneous mixed elastic inner layer 14 through the homogeneous mixed inlet 12, raw liquid to be rectified enters the self-expanding homogeneous mixed elastic inner layer 14 through the homogeneous mixed inlet 12 to form homogeneous mixed liquid, the homogeneous mixed liquid continuously enters the homogeneous mixed liquid, the homogeneous mixed liquid gradually expands and expands from the telescopic homogeneous mixed elastic inner layer 14, slides to the self-expanding homogeneous mixed rigid shell 11 along the homogeneous mixed outlet 9 and the homogeneous mixed inlet 12, the self-expanding homogeneous mixed elastic inner layer 14 is continuously expanded under the pressure of the homogeneous mixed liquid, the electromagnetic control valve I23 is opened, the homogeneous mixed liquid in the self-expanding homogeneous mixed elastic inner layer 14 rapidly impacts the multi-layer inverted triangular homogeneous self-counterweight progressive rectification tower 2 through the homogeneous mixed outlet 9 under the extrusion of the self-expanding homogeneous mixed liquid, and rises step by step along the multi-layer inverted triangular eddy current type homogeneous rectification layer 19, the homogeneous mixed liquid is taken as a flow channel through a plurality of groups of multilayer inverted triangular vortex type through holes 15 arranged in a trapezoidal structure with a wide lower part and a narrow upper part, so that the homogeneous mixed liquid is promoted to form a local vortex to increase the probability of separating volatile matters; heating pipe 20 heats inside medicinal soybean oil, promotes volatilizing of volatile matter, and autologous counter weight formula rectification mist catching piece 3 reduces the droplet and smugglies secretly, forms local polymerization through counter weight formula polymerization tank 16 simultaneously, carries out the separation of homogeneous mixture through arc balancing weight 17 during the polymerization, promotes the realization of rectification effect in a gathering.
The present invention and its embodiments have been described above, and the description is not intended to be limiting, and the drawings are only one embodiment of the present invention, and the actual structure is not limited thereto. In summary, those skilled in the art should appreciate that they can readily use the disclosed conception and specific embodiments as a basis for designing or modifying other structures for carrying out the same purposes of the present invention without departing from the spirit and scope of the invention as defined by the appended claims.
Claims (6)
1. A medicinal soybean oil rectification equipment which is characterized in that: the device comprises a multilayer inverted triangular vortex type step-by-step homogeneous rectification part, a multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, a self-counterweight type rectification foam catching part, a tower plate and a self-telescopic homogeneous mixing component, wherein the self-telescopic homogeneous mixing component is connected with the lower end of the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, the tower plate is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, the multilayer inverted triangular vortex type step-by-step homogeneous rectification part is arranged on the tower plate, the multilayer inverted triangular vortex type step-by-step homogeneous rectification part is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, and the self-counterweight type foam catching part is detachably arranged at the upper end of the multilayer inverted triangular vortex type homogeneous self-counterweight rectification tower; the self-telescopic homogeneous mixing assembly comprises a homogeneous mixing elastic part fixing seat, a self-telescopic homogeneous mixing elastic part and a cooling part, wherein the self-telescopic homogeneous mixing elastic part is arranged on the homogeneous mixing elastic part fixing seat, and the cooling part is connected with the self-telescopic homogeneous mixing elastic part; the self-telescopic homogeneous mixing elastic part comprises a homogeneous mixing outlet, a first limiting part, a self-telescopic homogeneous mixing rigid shell, a homogeneous mixing inlet, a second limiting part and a self-telescopic homogeneous mixing elastic inner layer, the self-telescopic homogeneous mixing rigid shell is arranged on the homogeneous mixing elastic part fixing seat, the homogeneous mixing outlet and the homogeneous mixing inlet are arranged on the self-telescopic homogeneous mixing rigid shell, the self-telescopic homogeneous mixing elastic inner layer is arranged in the self-telescopic homogeneous mixing rigid shell, the self-telescopic homogeneous mixing elastic inner layer is arranged on the homogeneous mixing outlet and the homogeneous mixing inlet, the first limiting piece and the second limiting piece are arranged in the self-telescopic homogeneous mixing elastic inner layer, the first limiting piece is arranged on the homogeneous mixing discharge port, the limiting piece II is arranged on the homogeneous mixing inlet, and the cooling piece is connected with the self-telescopic homogeneous mixing elastic inner layer through the homogeneous mixing inlet; a plurality of groups of inverted triangular vortex type through holes are uniformly arranged in the multilayer inverted triangular vortex type step-by-step homogeneous rectification piece at equal intervals; the self-counterweight type rectification foam catching part is arranged in an arc shape, the self-counterweight type rectification foam catching part is provided with a counterweight type polymerization groove, an arc-shaped counterweight block and a self-counterweight type rectification foam catching mesh hole, the self-counterweight type rectification foam catching mesh hole is in a trapezoidal arrangement with a narrow lower part and a wide upper part, the self-counterweight type rectification foam catching mesh hole is provided with a plurality of groups, the plurality of groups of self-counterweight type rectification foam catching mesh holes are uniformly arranged on the self-counterweight type rectification foam catching part at equal intervals, the counterweight type polymerization groove is arranged on the self-counterweight type rectification foam catching part and is close to the self-counterweight type rectification foam catching mesh hole, the counterweight type polymerization groove is provided with a plurality of groups, the counterweight type polymerization groove is arranged on the counterweight type rectification foam catching part at equal intervals, the arc-shaped counterweight block is arranged in the counterweight type polymerization groove and is close to the counterweight type rectification foam catching mesh hole, and the arc-shaped counterweight block is provided with, and the arc-shaped balancing weights of a plurality of groups are matched and arranged in the counterweight type polymerization tank.
2. The medicinal soybean oil rectification equipment according to claim 1, characterized in that: the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower is internally provided with a multilayer inverted triangular vortex homogeneous step-by-step rectifying layer, a heating conduit, a steam outlet pipe and a return pipe, the heating conduit is arranged at the lower end in the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower, the multilayer inverted triangular vortex type step-by-step homogeneous rectification layer is arranged in the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectification tower, the multilayer inverted triangular vortex step-by-step homogeneous rectifying layer is provided with a plurality of groups, the plurality of groups of multilayer inverted triangular vortex step-by-step homogeneous rectifying layers are arranged in the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower at intervals, the multilayer inverted triangular vortex step-by-step homogeneous rectification piece is arranged in the multilayer inverted triangular vortex step-by-step homogeneous rectification layer, the steam outlet pipe and the return pipe are arranged at the upper end of the multilayer inverted triangular vortex type homogeneous self-counterweight step-by-step rectifying tower.
3. The medicinal soybean oil rectification equipment according to claim 1, characterized in that: the homogeneous mixing discharge port is arranged on the side wall of the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower and is close to the bottom wall of the multilayer inverted triangular vortex homogeneous self-counterweight step-by-step rectifying tower.
4. The medicinal soybean oil rectification equipment according to claim 1, characterized in that: an electromagnetic control valve I is arranged in the homogeneous mixing outlet, and an electromagnetic control valve II is arranged in the homogeneous mixing inlet.
5. The medicinal soybean oil rectification equipment according to claim 1, characterized in that: the vertical section of the multilayer inverted triangular vortex step-by-step homogeneous rectification piece is in a trapezoidal arrangement.
6. The medicinal soybean oil rectification equipment according to claim 1, characterized in that: and the cooling piece is provided with a drop-shaped liquid inlet and a drop-shaped solid outlet, and the drop-shaped solid outlet is connected with the homogeneous mixing inlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110357926.6A CN112915568A (en) | 2021-04-01 | 2021-04-01 | Medicinal soybean oil rectifying equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110357926.6A CN112915568A (en) | 2021-04-01 | 2021-04-01 | Medicinal soybean oil rectifying equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN112915568A true CN112915568A (en) | 2021-06-08 |
Family
ID=76173863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110357926.6A Pending CN112915568A (en) | 2021-04-01 | 2021-04-01 | Medicinal soybean oil rectifying equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112915568A (en) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB867852A (en) * | 1958-05-08 | 1961-05-10 | Drew & Co Inc E F | Improvements in or relating to the modification of fatty oils |
CN1962012A (en) * | 2006-11-01 | 2007-05-16 | 褚雅志 | Bubble cap integrated stereo sieve plate |
US20080275277A1 (en) * | 2006-10-27 | 2008-11-06 | Peter Kalagias | Processes for isolating or purifying propylene glycol, ethylene glycol and products produced therefrom |
CN101337880A (en) * | 2007-07-06 | 2009-01-07 | 通渭县晓铃商贸有限责任公司 | Process for extracting alpha-linolenic acid |
CN102224856A (en) * | 2011-05-25 | 2011-10-26 | 东北农业大学 | Method for synchronously extracting soybean oil and protein concentrate |
CN203899191U (en) * | 2014-06-06 | 2014-10-29 | 宜宾石平香料有限公司 | Rectifying tower |
CN204017417U (en) * | 2014-05-30 | 2014-12-17 | 浙江富士特集团有限公司 | A kind of rectifying column for purifying silicon tetrachloride |
CN106807104A (en) * | 2017-03-22 | 2017-06-09 | 中国石油大学(华东) | A kind of low pressure drop liquid header of suitable large-scale tower |
CN207237335U (en) * | 2017-08-07 | 2018-04-17 | 青岛科技大学 | One kind atomization column plate and atomization column plate rectifying column |
-
2021
- 2021-04-01 CN CN202110357926.6A patent/CN112915568A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB867852A (en) * | 1958-05-08 | 1961-05-10 | Drew & Co Inc E F | Improvements in or relating to the modification of fatty oils |
US20080275277A1 (en) * | 2006-10-27 | 2008-11-06 | Peter Kalagias | Processes for isolating or purifying propylene glycol, ethylene glycol and products produced therefrom |
CN1962012A (en) * | 2006-11-01 | 2007-05-16 | 褚雅志 | Bubble cap integrated stereo sieve plate |
CN101337880A (en) * | 2007-07-06 | 2009-01-07 | 通渭县晓铃商贸有限责任公司 | Process for extracting alpha-linolenic acid |
CN102224856A (en) * | 2011-05-25 | 2011-10-26 | 东北农业大学 | Method for synchronously extracting soybean oil and protein concentrate |
CN204017417U (en) * | 2014-05-30 | 2014-12-17 | 浙江富士特集团有限公司 | A kind of rectifying column for purifying silicon tetrachloride |
CN203899191U (en) * | 2014-06-06 | 2014-10-29 | 宜宾石平香料有限公司 | Rectifying tower |
CN106807104A (en) * | 2017-03-22 | 2017-06-09 | 中国石油大学(华东) | A kind of low pressure drop liquid header of suitable large-scale tower |
CN207237335U (en) * | 2017-08-07 | 2018-04-17 | 青岛科技大学 | One kind atomization column plate and atomization column plate rectifying column |
Non-Patent Citations (4)
Title |
---|
冯骉等: "《食品工程原理》", 31 August 2019, 中国轻工业出版社 * |
刘春江等: "塔板上流型变化对板效率影响的计算传质学", 《化工学报》 * |
吴俊生等: "《分离工程》", 30 August 1992, 华东化工学院出版社 * |
张木全等: "《化工原理》", 28 February 2000, 华南理工大学出版社 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU684157B2 (en) | Column for counter-currently contacting gas and liquid | |
CN100453945C (en) | Improved evaporative heat exchanger and method | |
EP2829308B1 (en) | Liquid dispensing device | |
US9630154B2 (en) | Apparatus and method for contacting a gas and a liquid | |
US20120111762A1 (en) | Enhanced capacity, reduced turbulence, trough-type liquid collector trays | |
CN113908578A (en) | Plate type fractionating tower | |
CN110170178A (en) | A kind of condensing unit distilling tower top | |
CN107917638B (en) | Flow equalizing plate, oil separator, condenser and flash evaporator | |
CN112915568A (en) | Medicinal soybean oil rectifying equipment | |
CN108826760A (en) | The multistage flooded evaporator of spiracular plate structure and anti-absorbing gas belt liquid | |
CN109985576B (en) | Gas-liquid mass transfer system | |
US5283012A (en) | Self-balancing hot water distribution system for multi-level cooling tower | |
SE541197C2 (en) | Venting device at a reservoir for a hydraulic system | |
CN103759554B (en) | Semi-closed spray cooler | |
RU182052U1 (en) | Gas-liquid separator | |
CN208154881U (en) | Liquid distributor with two-stage liquid separation chamber structure | |
CN216011920U (en) | Steam inlet buffering device of shell-and-tube condenser | |
CN216458756U (en) | Novel graphite high-gas-speed riser type liquid distributor | |
CN105289031A (en) | Falling-film jet column tray | |
CN117531319B (en) | Water-gas separation equipment | |
CN217031306U (en) | Compound water condensation oil smoke purifies integrated kitchen | |
CN220766913U (en) | Oil-water separator, vegetable oil separation device and vegetable oil preparation system | |
CN221173027U (en) | Concentrating condenser | |
CN220572674U (en) | Defoaming device of distillation kettle | |
CN216125204U (en) | Fractional heat exchange reflux rectifying tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210608 |