CN216877920U - High-yield and high-efficiency turpentine oil recovery system - Google Patents
High-yield and high-efficiency turpentine oil recovery system Download PDFInfo
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- CN216877920U CN216877920U CN202220641086.6U CN202220641086U CN216877920U CN 216877920 U CN216877920 U CN 216877920U CN 202220641086 U CN202220641086 U CN 202220641086U CN 216877920 U CN216877920 U CN 216877920U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract
The utility model discloses a high-yield and high-efficiency turpentine recovery system, which relates to the technical field of chemical equipment and comprises a tank body, wherein a collecting pipe penetrates through the upper surface of the tank body, the top end of the collecting pipe is provided with a condenser and an air inlet on the surface of the condenser, the bottom end of the condenser is communicated with a mechanical drain valve, steam enters through the top end of a condensing straight pipe, condensed water is directly led into the collecting pipe through a guide pipe under the action of a steam drain valve, meanwhile, residual steam enters into a condensing coil, airflow enters between a shell and a separating cylinder through the air inlet, the airflow flows to the inner wall of the separating cylinder along with the surface of the separating cylinder until the airflow is discharged through an air outlet, the step of internal two-section condensation is realized, the steam enters the front surface of the shell and is cooled, a three-section cooling mode is comprehensively adopted, the condensing efficiency is higher, and can also keep good recovery effect on the internal turpentine and improve the yield of the turpentine.
Description
Technical Field
The utility model belongs to the technical field of forestry equipment, and particularly relates to a high-yield and high-efficiency turpentine oil recovery system.
Background
Rosin is a natural secretion in pine trees, has wide application, can be used in the fields of medicine, industry and the like, is usually obtained by distilling rosin when the rosin is processed, and can be mixed with steam in a distillation kettle in the distillation process to obtain liquid turpentine after condensation. As the current industrial treatment process of this kind of raw materials, need collect the turpentine in the steam, make it so both to ensure can used repeatedly after the distilled water handles, the turpentine also can improve the added value simultaneously, nevertheless need to condense steam and retrieve through oil water separator at present in carrying out the turpentine recovery process, nevertheless in with steam condensation process, traditional condenser often needs a plurality of cooperations side can reach suitable condensation effect, however the great and efficiency of most bulk of this kind of mode receives the influence.
The above background disclosure is only for the purpose of aiding understanding of the inventive concepts and solutions of the present invention, and it is not necessary for them to belong to the prior art of this patent application, and it should not be used for evaluating the novelty and inventive step of this application in the case that there is no clear evidence that the above contents are disclosed at the filing date of this patent application.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In order to overcome the defects in the prior art, the utility model provides a high-yield and high-efficiency turpentine recovery system, and solves the problem that the efficiency is influenced due to the fact that a condensing device for turpentine recovery is large in size and low in integration level.
(II) technical scheme
In order to achieve the purpose, the utility model provides the following technical scheme:
the utility model provides a high-yield efficient turpentine recovery system, includes a jar body, the upper surface of jar body runs through the intercommunication and has the collecting pipe, the top of collecting pipe is provided with condenser and the air intake on condenser surface thereof, the bottom intercommunication of condenser has mechanical trap.
The top fixedly connected with of jar internal wall is gone up a layering section of thick bamboo, the lower fixed surface of going up a layering section of thick bamboo is connected with the accumulator, the lower surface of accumulator runs through and is fixed with a next layering section of thick bamboo, the surface joint of the jar body has blast pipe, recovery tank and permanent water pipe.
As a further scheme of the utility model: the condenser is including setting up in the casing of jar body top, shells inner wall's last fixed surface is connected with separates a section of thick bamboo, it is provided with the condensation straight tube to run through in the section of thick bamboo to separate, the bottom of condensation straight tube runs through fixed connection at the lower surface of casing, the surface spiral of separating a section of thick bamboo is coiled there is the condensation coil, the bottom of condensation coil is linked together with the steam interface of mechanical trap.
As a further scheme of the utility model: the lower surface of the tank body is fixedly provided with a deposition bin in a penetrating way, and the lower surface of the inner wall of the deposition bin is fixedly connected with a drain pipe.
As a further scheme of the utility model: the water outlet of the mechanical trap is communicated with a flow guide pipe, one end of the flow guide pipe is communicated with the surface of the collecting pipe, the top end of the condensing coil pipe is communicated with the top end of the collecting pipe, an air outlet is formed in the upper surface of the shell, and the condensing straight pipe penetrates through the air outlet.
As a further scheme of the utility model: one end of the exhaust pipe is communicated with the top end of the upper layering barrel, one end of the recovery tank is communicated with the inner wall of the recovery tank, and the lower surface of the inner wall of the recovery tank is a conical inclined surface.
As a further scheme of the utility model: the air intake includes the air-collecting cover of fixed connection at the casing upper surface, the inner wall of air-collecting cover is provided with the fan by motor drive, one side of air-collecting cover is provided with the filter screen.
As a further scheme of the utility model: the bottom end of the separating cylinder is in a non-contact state with the inner wall of the shell, and the air outlet is located at the axial position of the separating cylinder.
(III) advantageous effects
Compared with the prior art, the utility model has the beneficial effects that:
1. the utility model provides a turpentine recovery system, which is provided with a shell, a condensation straight pipe, a tank body, a condensation coil pipe, a mechanical drain valve, a separation cylinder and an air outlet, when in use, steam enters through the top end of the condensation straight pipe, most of the steam is condensed under the action of the condensation straight pipe, condensed water is directly led into a collecting pipe through a flow guide pipe under the action of the steam drain valve, residual steam enters into the condensation coil pipe and then enters into the top end of the collecting pipe under the action of gas after being condensed, in the condensation process, airflow enters between the shell and the separation cylinder through an air inlet and cools the condensation coil pipe, and meanwhile, the airflow flows to the inner wall of the separation cylinder along the surface of the separation cylinder until being discharged through the air outlet, the method can realize the step of internal two-section condensation, and simultaneously, the condensation straight pipe can be blown along the air outlet, the steam enters the front surface air flow of the shell to cool the shell, so that a three-section cooling mode is comprehensively realized, the condensation effect is guaranteed, the structure is simple, and the condensation efficiency is higher.
2. The utility model relates to a turpentine recovery system, which is characterized in that a collecting pipe, a recovery tank, an upper layering cylinder, a lower layering cylinder, an exhaust pipe, a recovery pipe and a constant water pipe are arranged, when in use, solution with a certain height is pre-filled in a tank body, the solution keeps the liquid level flush with the top end of the lower layering cylinder under the action of the constant water pipe, the condensate enters the lower layering cylinder along with the inflow of steam and condensate through the collecting pipe, turpentine oil floats on the liquid level and is higher than the liquid level, water is mixed with the solution at the bottom, the solution is increased by the excessive water, the excessive water is discharged through the constant water pipe, the turpentine oil higher than the water level keeps a certain height under the convergence of the lower layering cylinder and is collected through the recovery pipe, and the air flow is discharged through the exhaust pipe on the surface of the upper layering cylinder, so that the turpentine oil recovery system can keep a good recovery effect on the internal turpentine oil, the yield of turpentine is improved.
3. This turpentine recovery system, through setting up a jar body, permanent water pipe, deposit storehouse and blow off pipe, when using, its comdenstion water mixes the back with the solution of jar internal portion, and the deposit storehouse of its bottom can be collected the impurity of inside, prevents to discharge through permanent water pipe, when needs simultaneously, discharges the clearance through the solution of blow off pipe with jar internal portion.
Drawings
FIG. 1 is a schematic perspective view of the present invention;
FIG. 2 is a schematic cross-sectional view of a condenser according to the present invention;
FIG. 3 is a schematic three-dimensional sectional structure of the can body of the present invention;
FIG. 4 is a schematic sectional view of the present invention.
In the figure: 1 tank body, 2 collecting pipes, 3 condensers, 31 shells, 32 condensation straight pipes, 33 separating cylinders, 34 air outlets, 35 condensation coils, 4 air inlets, 41 air collecting covers, 42 fans, 5 upper layering cylinders, 6 recovery tanks, 7 lower layering cylinders, 8 deposition bins, 9 sewage pipes, 10 exhaust pipes, 11 recovery pipes, 12 constant water pipes, 13 mechanical drain valves and 14 flow guide pipes.
Detailed Description
The technical solution of the present patent will be described in further detail with reference to the following embodiments.
As shown in fig. 1 to 4, the present invention provides a technical solution: the utility model provides a high yield efficient turpentine recovery system, includes jar body 1, its characterized in that: the upper surface of the tank body 1 is communicated with a collecting pipe 2 in a penetrating way, the top end of the collecting pipe 2 is provided with a condenser 3 and an air inlet 4 on the surface of the condenser 3, and the bottom end of the condenser 3 is communicated with a mechanical drain valve 13.
The top fixedly connected with of the 1 inner wall of jar body is superior to a layering section of thick bamboo 5, and the lower fixed surface of an upper layering section of thick bamboo 5 is connected with accumulator 6, and the lower surface of accumulator 6 runs through and is fixed with a lower layering section of thick bamboo 7, and the surface joint of the jar body 1 has blast pipe 10, recovery jar and constant water pipe 12.
Specifically, as shown in fig. 1 and 4, a deposition chamber 8 is fixedly penetrated through the lower surface of the tank body 1, a sewage discharge pipe 9 is fixedly connected to the lower surface of the inner wall of the deposition chamber 8, the air inlet 4 includes an air collecting cover 41 fixedly connected to the upper surface of the housing 31, a fan 42 driven by a motor is arranged on the inner wall of the air collecting cover 41, and a filter screen is arranged on one side of the air collecting cover 41.
Through setting up deposit storehouse 8, some impurity that deposit storehouse 8 can keep producing inside solution long-term use are collected, can effectively keep the effect and the clean degree of inside separation, be convenient for carry out fine collection reuse through permanent water pipe 12 exhaust solution, through setting up blow off pipe 9, blow off pipe 9 can cooperate down can be convenient for unify clearance and replacement to the solution of jar body 1 inside for a period of time, through setting up air-collecting cover 41, air-collecting cover 41 can keep the effect that good air current assembles when using, make it cooperate inside fan 42 effect down to keep injecting into casing 31 after the gas pressurization, keep the inside gas velocity of flow of casing 31 to keep at a suitable speed, guarantee refrigerated effect.
Specifically, as shown in fig. 2 and fig. 3, the condenser 3 includes a housing 31 disposed above the tank 1, an upper surface of an inner wall of the housing 31 is fixedly connected with a separation cylinder 33, a condensation straight pipe 32 penetrates through the separation cylinder 33, a bottom end of the condensation straight pipe 32 penetrates through a lower surface of the housing 31, a surface spiral coil of the separation cylinder 33 is wound with a condensation coil 35, a bottom end of the condensation coil 35 is communicated with a steam interface of the mechanical trap 13, a water outlet of the mechanical trap 13 is communicated with a flow guide pipe 14, one end of the flow guide pipe 14 is communicated with a surface of the flow guide pipe 2, a top end of the condensation coil 35 is communicated with a top end of the flow guide pipe 2, an air outlet 34 is disposed on an upper surface of the housing 31, the condensation straight pipe 32 penetrates through the air outlet 34, a bottom end of the separation cylinder 33 is in a non-contact state with the inner wall of the housing 31, and the air outlet 34 is located at an axial position of the separation cylinder 33.
By arranging the shell 31, the shell 31 can keep the inside of the condenser 3 to play a good protection effect, by arranging the separation cylinder 33, the separation cylinder 33 can keep an effect of guiding the flow of the air flow inside, so that the directional flow effect is kept, by arranging the condensation straight pipe 32, one section of the surface of the condensation straight pipe 32, which is positioned outside the shell 31, can be cooled in the external environment under the blowing of the air flow, and the effect of primary cooling and condensation is achieved, by arranging the condensation coil 35, the stroke of the condensation coil 35 is longer compared with that of the condensation straight pipe 32, the contact surface and the time of the condensation coil are longer, the condensation coil is directly contacted with the air flow entering the shell 31 initially, the best cooling effect is achieved, the sufficient condensation of the steam to be participated in is kept, by arranging the air outlet 34, the air outlet 34 can keep the gas inside discharged, and simultaneously the gas is blown along a certain direction, heat dissipation is maintained.
The working principle of the utility model is as follows:
steam enters through the top end of the condensation straight pipe 32, most of the steam is condensed under the action of the condensation straight pipe 32, condensed water is directly led into the collecting pipe 2 through the guide pipe 14 under the action of the steam trap, meanwhile, residual steam enters into the condensation coil 35 and then enters the top end of the collecting pipe 2 under the action of gas after condensation, in the condensation process, airflow enters between the shell 31 and the separating cylinder 33 through the air inlet 4 and cools the condensation coil 35, meanwhile, the airflow flows to the inner wall of the separating cylinder 33 along with the surface of the separating cylinder 33 until the airflow is discharged through the air outlet 34, when the steam condensing tank is used, a certain height of solution is pre-filled in the tank body 1, the liquid level of the solution is kept flush with the top end of the lower layering cylinder 7 under the action of the constant water pipe 12, and the condensate enters into the lower layering cylinder 7 along with the inflow of the steam and the condensate through the collecting pipe 2, the turpentine oil floats on the liquid level and is higher than the liquid level, the water body is mixed with the solution at the bottom, the water body which is higher than the liquid level increases the solution, the surplus water body is discharged through a constant water pipe 12, the turpentine oil which is higher than the water level keeps a certain height under the convergence of a lower layering cylinder 7 and is collected through a recovery pipe 11, meanwhile, the air flow is discharged through an exhaust pipe 10 on the surface of an upper layering cylinder 5, after the condensate water is mixed with the solution in the tank body 1, a deposition bin 8 at the bottom of the turpentine oil collects impurities in the tank body 1 and prevents the impurities from being discharged through the constant water pipe 12, and when needed, the solution in the tank body 1 is discharged and cleaned through a drain pipe 9.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
Although the preferred embodiments of the present patent have been described in detail, the present patent is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present patent within the knowledge of those skilled in the art.
Claims (8)
1. The utility model provides a high yield efficient turpentine recovery system, includes jar body (1), its characterized in that: the upper surface of the tank body (1) is communicated with a collecting pipe (2) in a penetrating way, the top end of the collecting pipe (2) is provided with a condenser (3) and an air inlet (4) on the surface of the condenser (3), and the bottom end of the condenser (3) is communicated with a mechanical drain valve (13);
the top of the inner wall of the tank body (1) is fixedly connected with an upper layering cylinder (5), the lower surface of the upper layering cylinder (5) is fixedly connected with a recovery tank (6), the lower surface of the recovery tank (6) is fixedly penetrated with a lower layering cylinder (7), and an exhaust pipe (10), a recovery tank and a constant water pipe (12) are clamped on the surface of the tank body (1);
condenser (3) is including setting up in casing (31) of jar body (1) top, the last fixed surface of casing (31) inner wall is connected with separates a section of thick bamboo (33), it is provided with condensation straight tube (32) to run through in separating a section of thick bamboo (33), the bottom of condensation straight tube (32) runs through fixed connection at the lower surface of casing (31), the surperficial spiral of separating a section of thick bamboo (33) is coiled there is condensation coil pipe (35), the bottom of condensation coil pipe (35) is linked together with the steam interface of mechanical trap (13).
2. The high-yield and high-efficiency turpentine recovery system according to claim 1, characterized in that: the lower surface of the tank body (1) penetrates through and is fixed with a deposition bin (8), and the lower surface of the inner wall of the deposition bin (8) is fixedly connected with a drain pipe (9).
3. The high-yield high-efficiency turpentine oil recovery system according to claim 1, characterized in that: the water outlet of the mechanical trap (13) is communicated with a flow guide pipe (14), one end of the flow guide pipe (14) is communicated with the surface of the collecting pipe (2), the top end of the condensing coil pipe (35) is communicated with the top end of the collecting pipe (2), an air outlet (34) is formed in the upper surface of the shell (31), and the condensing straight pipe (32) penetrates through the air outlet (34).
4. The high-yield and high-efficiency turpentine recovery system according to claim 1, characterized in that: one end of the exhaust pipe (10) is communicated with the top end of the upper layered cylinder (5), and one end of the recovery tank is communicated with the inner wall of the recovery tank (6).
5. The high-yield and high-efficiency turpentine recovery system according to claim 4, characterized in that: the lower surface of the inner wall of the recovery tank (6) is a conical inclined plane.
6. The high-yield and high-efficiency turpentine recovery system according to claim 3, characterized in that: the air inlet (4) comprises an air collecting cover (41) fixedly connected to the upper surface of the shell (31), and a fan (42) driven by a motor is arranged on the inner wall of the air collecting cover (41).
7. The high-yield and high-efficiency turpentine recovery system according to claim 6, characterized in that: and a filter screen is arranged on one side of the air collecting cover (41).
8. The high-yield and high-efficiency turpentine recovery system according to claim 3, characterized in that: the bottom end of the separating cylinder (33) is in a non-contact state with the inner wall of the shell (31), and the air outlet (34) is located at the axial position of the separating cylinder (33).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220641086.6U CN216877920U (en) | 2022-03-23 | 2022-03-23 | High-yield and high-efficiency turpentine oil recovery system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220641086.6U CN216877920U (en) | 2022-03-23 | 2022-03-23 | High-yield and high-efficiency turpentine oil recovery system |
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| CN216877920U true CN216877920U (en) | 2022-07-05 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115253358A (en) * | 2022-07-14 | 2022-11-01 | 丽水学院 | Raw material extraction condenser for catalyst preparation |
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- 2022-03-23 CN CN202220641086.6U patent/CN216877920U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115253358A (en) * | 2022-07-14 | 2022-11-01 | 丽水学院 | Raw material extraction condenser for catalyst preparation |
| CN115253358B (en) * | 2022-07-14 | 2023-05-30 | 丽水学院 | Raw material extraction condenser for catalyst preparation |
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