CN217555819U

CN217555819U - Device for preparing smoking fluid and co-producing active carbon by pyrolysis of hawthorn seeds

Info

Publication number: CN217555819U
Application number: CN202221845573.0U
Authority: CN
Inventors: 陈浩然; 陈佰亿; 姜翠梅
Original assignee: Chengde Benduobao Biotechnology Co ltd
Current assignee: Chengde Benduobao Biotechnology Co ltd
Priority date: 2022-07-18
Filing date: 2022-07-18
Publication date: 2022-10-11
Anticipated expiration: 2032-07-18

Abstract

The utility model discloses a device of smoked liquid coproduction active carbon is prepared in hawthorn nuclear pyrolysis, including drawing jar and condensing tank, draw jar top and install sealed lid, the position that is close to the top on drawing the tank shell is provided with the control box, control box below is provided with gets the bin gate, it is provided with the dry distillation jar to draw jar interior top, the dry distillation jar with draw the smoke exhaust passage of installing on the tank shell and be linked together, smoke exhaust passage through the constant pressure valve with the condensing tank is connected, draw the tank bottom and install the condensate discharge valve, the outside of dry distillation jar encircle install with the electric heat ring one that the control box electricity is connected, this kind of device of smoked liquid coproduction active carbon is prepared in hawthorn nuclear pyrolysis, can carry out the dry distillation to the hawthorn nucleus when drawing, carries out the activation with the residue after the dry distillation and handles to coproduction hawthorn nuclear dry distillation liquid and active carbon, easy operation, convenient, high efficiency can effectively improve economic benefits.

Description

Device for preparing smoking fluid and co-producing active carbon by pyrolysis of hawthorn seeds

Technical Field

The utility model relates to a hawthorn seed deep-processing equipment field specifically is a device of smoked liquid coproduction active carbon is prepared in hawthorn seed pyrolysis.

Background

Haw is a common fruit, hard in stone, thin in pulp, slightly sour and astringent in taste. The hawthorn fruit can be eaten as raw fruit or preserved fruit cake, can be used as medicine after being dried, is a special Chinese medicine and fruit tree species, has the functions of reducing blood fat, blood pressure, strengthening heart, resisting arrhythmia and the like, is also a good medicine for tonifying spleen, stimulating appetite, promoting digestion, removing stagnation, promoting blood circulation and reducing phlegm, and has good curative effects on chest and spleen fullness, hernia, blood stasis, amenorrhea and other diseases. The vitexin is a flavonoid compound in hawthorn, is a drug with strong anticancer effect, the extract of the vitexin has certain effects on inhibiting the growth, proliferation and infiltration and transfer of cancer cells in vivo, and hawthorn kernel dry distillation liquid has the effects of detoxifying, clearing damp, killing parasites and relieving itching, and is commonly used for pruritus vulvae and leukorrhagia caused by downward flow of damp toxin; patients with mycotic vaginitis and nonspecific vaginitis, therefore, the whole body of hawthorn is good and is an excellent commercial crop.

At present, after hawthorn seeds are subjected to dry distillation, residual carbonization residues are generally directly discarded, so that not only is great waste caused, but also the environment is easily polluted, and the enterprise benefit is reduced.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a device of smoked liquid coproduction active carbon is prepared in hawthorn nuclear pyrolysis to solve the waste and the environmental pollution's that directly abandon hawthorn nuclear dry distillation residue and lead to problem.

The technical scheme of the utility model is realized like this: the utility model provides a device of smoked liquid coproduction active carbon is prepared in pyrolysis of hawthorn nucleus, is including drawing jar and condensing tank, draw tank deck portion and install sealed lid, it is provided with the control box to draw the position that is close to the top on the jar shell, the control box below is provided with gets the bin gate, it is provided with the dry distillation jar to draw jar interior top, the dry distillation jar with draw the exhaust passage of installing on the jar casing and be linked together, exhaust passage through the constant pressure valve with the condensing tank is connected, draw tank deck portion and install the condensate blow-off valve, the outside of dry distillation jar encircle install with the electric heat ring one that the control box electricity is connected, dry distillation jar bottom is connected with the activation jar through the unloading solenoid valve, one side and the intake pipe of activation jar are linked together, the opposite side and the blast pipe of activation jar are linked together, the outside of activation jar encircle install with the electric heat ring two that the control box electricity is connected, two internally mounted of electric heat ring have activation rack net, activation rack net with the bottom height of getting the bin gate is kept level, the sediment valve is installed to two bottoms of electric heat ring.

Preferably, the bottom of the extracting tank and the bottom of the condensate draining valve are fixedly provided with fixed bases.

Preferably, a first temperature sensor electrically connected with the control box is installed on the top of the retort, and a second temperature sensor and a carbon dioxide sensor electrically connected with the control box are installed on the top of the activation tank.

Preferably, the air inlet pipe the exhaust pipe the smoke exhaust passage constant pressure valve is all installed with the solenoid valve that the control box electricity is connected.

Preferably, the material taking door is in transmission connection with the extracting tank through a sealing hinge.

Preferably, heat insulation cotton is filled between the extraction tank and the dry distillation tank, and heat insulation cotton is filled between the extraction tank and the activation tank.

Preferably, the bottom of the dry distillation tank and the bottom of the activation tank are both arc-shaped structures.

Preferably, the blanking electromagnetic valve is electrically connected with the control box.

By adopting the technical scheme, the beneficial effects of the utility model are that:

the device for preparing the smoke liquid and co-producing the activated carbon by pyrolyzing the hawthorn seeds can perform dry distillation extraction on the hawthorn seeds and simultaneously perform activation treatment on residues after the dry distillation, so that the hawthorn seed dry distillation liquid and the activated carbon are simultaneously produced, the operation is simple, convenient and efficient, and the economic benefit can be effectively improved.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the description below are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without inventive labor.

Fig. 1 is a front view of the present invention;

fig. 2 is the internal structure view of the extraction tank of the present invention.

Wherein: 1. an extraction tank; 2. a sealing cover; 3. a control box; 4. a material taking door; 5. an air inlet pipe; 6. a slag discharge valve; 7. an exhaust pipe; 8. a smoke evacuation channel; 9. a constant pressure valve; 10. a condensing tank; 11. a condensate drain valve; 12. a fixed base; 13. a retort; 14. a first electric heating coil; 15. a blanking electromagnetic valve; 16. an activation tank; 17. a second electric heating coil; 18. activating the trellis grids; 19. a first temperature sensor; 20. a second temperature sensor; 21. a carbon dioxide sensor.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.

Referring to fig. 1-2, a device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels comprises an extraction tank 1 and a condensation tank 10, wherein a sealing cover 2 is installed at the top of the extraction tank 1, a control box 3 is arranged on the shell of the extraction tank 1 and close to the top, a material taking door 4 is arranged below the control box 3, a dry distillation tank 13 is arranged above the interior of the extraction tank 1, the dry distillation tank 13 is communicated with a smoke exhaust channel 8 installed on the shell of the extraction tank 1, the smoke exhaust channel 8 is connected with the condensation tank 10 through a constant pressure valve 9, a condensate discharge valve 11 is installed at the bottom of the extraction tank 1, a first electric heating ring 14 electrically connected with the control box 3 is installed around the exterior of the dry distillation tank 13, the bottom of the dry distillation tank 13 is connected with an activation tank 16 through a blanking electromagnetic valve 15, one side of the activation tank 16 is communicated with an air inlet pipe 5, the other side of the activation tank 16 is communicated with an exhaust pipe 7, a second electric heating ring 17 electrically connected with the control box 3 is installed around the exterior of the activation tank 16, an activation shelf grid 18 is installed inside the activation tank 17, the activation shelf grid 18 is kept at the same height as the bottom of the material taking door 4, and the bottom of the valve 6 is installed at the same height.

Specifically, draw

jar

1, 11 bottom fixed mounting of condensate drain valve have unable adjustment base 12, set up like this and will draw jar 1, condensate drain valve 11 to couple together through unable adjustment base 12, make this device form a whole to improve overall stability.

Specifically, the temperature sensor 19 that 3 electricity of control box are connected is installed at dry distillation jar 13 top, the two 20 and the carbon dioxide sensor 21 of temperature sensor that 3 electricity of control box are connected are installed at activation jar 16 top, set up the dry distillation temperature that can real time monitoring dry distillation jar 13 and activation jar 16 like this, and feed back and show to control box 3, make things convenient for the staff to look over, carbon dioxide concentration in the while can real time monitoring activation jar 16, make things convenient for the staff in the activation jar 16 carbon dioxide concentration back up to standard, close intake pipe 5 and blast pipe 7.

Specifically, all install the solenoid valve of being connected with control box 3 electricity on intake pipe 5, blast pipe 7, smoke exhaust passage 8, the constant pressure valve 9, set up like this and be convenient for by the automatic control intake pipe 5 of control box 3, blast pipe 7, smoke exhaust passage 8, opening and closing of constant pressure valve 9 to improve automation, the intelligent performance of this device.

It is specific, get bin gate 4 and draw jar 1 and be connected through sealed hinge drive, set up like this and can guarantee to get bin gate 4 and draw jar 1 leakproofness, provide stable carbon dioxide environment for the production of active carbon.

Specifically, it has thermal-insulated cotton to fill between jar 1 and the dry distillation jar 13 of drawing, draws to fill between jar 1 and the activation jar 16 to have thermal-insulated cotton, sets up like this and can reduce the waste of heat, avoids the user to scald simultaneously.

Specifically, the bottoms of the dry distillation tank 13 and the activation tank 16 are both arc-shaped structures, so that materials in the dry distillation tank 13 and the activation tank 16 can be conveniently gathered, and blanking is convenient.

Specifically, the blanking electromagnetic valve 15 is electrically connected with the control box 3, so that the control box 3 can control the blanking electromagnetic valve 15 to be opened and closed conveniently, and the production line of dry distillation and activation is realized.

The working principle is as follows: when the device is used for processing the hawthorn kernels, the sealing cover 2 is opened, the hawthorn kernels to be processed are placed in the dry distillation tank 13, then the sealing cover 2 is closed, a working instruction is input by the control box 3, the control box 3 controls the first electric heating ring 14 to convert electric energy into heat energy, under the closed environment of the dry distillation tank 13, dry distillation extraction is carried out on the hawthorn kernels, steam is guided into the condensation tank 10 through the smoke exhaust channel 8 and the constant pressure valve 9 to carry out condensation processing, hawthorn kernel dry distillation liquid generated after condensation is discharged through the condensate discharge valve 11, after the hawthorn kernel dry distillation operation is completed, the control box 3 controls the blanking electromagnetic valve 15 to be opened, hawthorn kernel residues in the dry distillation tank 13 are poured into the activation tank 16 through the blanking electromagnetic valve 15 and fall on the activation shed grids 18, then the control box 3 controls the blanking electromagnetic valve 15 to be closed and controls the second electric heating ring 17 to be opened, carbon dioxide gas is injected into the activation tank 16 through the air inlet pipe 5, the carbon dioxide gas density is higher than that air is extruded from the exhaust pipe 7 until the carbon dioxide gas is contained in the activation tank 16, at the moment, the exhaust pipe 5 and the exhaust pipe 7 is closed, the activated carbon kernel dry distillation operation liquid provided by the electric heating ring 2, the active charcoal rings 17, the activated charcoal grid 18, and the activated charcoal kernel hot carbon particles are discharged through the activated charcoal grid, and the activated charcoal extraction is taken out, and the activated charcoal extraction grid, and the activated charcoal extraction is carried out, and the activated charcoal extraction.

The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims

1. A device for preparing smoking fluid and co-producing active carbon by pyrolysis of hawthorn kernels is characterized in that: including extracting jar (1) and condensing jar (10), sealed lid (2) are installed at extracting jar (1) top, the position that is close to the top on extracting jar (1) shell is provided with control box (3), control box (3) below is provided with gets bin gate (4), the top is provided with dry distillation jar (13) in extracting jar (1), dry distillation jar (13) with smoke exhaust passage (8) of installation on extracting jar (1) casing are linked together, smoke exhaust passage (8) through constant pressure valve (9) with condensing jar (10) are connected, extract jar (1) bottom and install condensate bleeder valve (11), the outside of dry distillation jar (13) is encircleed install with electric heating coil one (14) that control box (3) electricity is connected, dry distillation jar (13) bottom is connected with activation jar (16) through unloading solenoid valve (15), one side and intake pipe (5) of activation jar (16) are linked together, the opposite side and blast pipe (7) of activation jar (16) are linked together, activation jar (16) outside is encircleed install with electric heating coil (3) are connected with two grid racks (17), activation grid height 17) are held in the grid frame is got, and a slag discharge valve (6) is arranged at the bottom of the second electric heating ring (17).

2. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, wherein: the bottom of the extracting tank (1) and the bottom of the condensate discharging valve (11) are fixedly provided with a fixed base (12).

3. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, wherein: the top of the dry distillation tank (13) is provided with a first temperature sensor (19) electrically connected with the control box (3), and the top of the activation tank (16) is provided with a second temperature sensor (20) and a carbon dioxide sensor (21) electrically connected with the control box (3).

4. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, characterized in that: the air inlet pipe (5), the exhaust pipe (7), the smoke exhaust channel (8) and the constant pressure valve (9) are all provided with electromagnetic valves electrically connected with the control box (3).

5. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, wherein: the material taking door (4) is in transmission connection with the extracting tank (1) through a sealing hinge.

6. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, wherein: and heat insulation cotton is filled between the extraction tank (1) and the dry distillation tank (13), and heat insulation cotton is filled between the extraction tank (1) and the activation tank (16).

7. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, characterized in that: the bottoms of the dry distillation tank (13) and the activation tank (16) are both arc-shaped structures.

8. The device for preparing liquid smoke and co-producing activated carbon by pyrolysis of hawthorn kernels as claimed in claim 1, wherein: the blanking electromagnetic valve (15) is electrically connected with the control box (3).