CN219907483U - Fresh bamboo draining distillation equipment - Google Patents
Fresh bamboo draining distillation equipment Download PDFInfo
- Publication number
- CN219907483U CN219907483U CN202321587708.2U CN202321587708U CN219907483U CN 219907483 U CN219907483 U CN 219907483U CN 202321587708 U CN202321587708 U CN 202321587708U CN 219907483 U CN219907483 U CN 219907483U
- Authority
- CN
- China
- Prior art keywords
- tank
- dry distillation
- valve
- cooler
- passing
- 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.)
- Active
Links
- 235000017166 Bambusa arundinacea Nutrition 0.000 title claims abstract description 32
- 235000017491 Bambusa tulda Nutrition 0.000 title claims abstract description 32
- 241001330002 Bambuseae Species 0.000 title claims abstract description 32
- 235000015334 Phyllostachys viridis Nutrition 0.000 title claims abstract description 32
- 239000011425 bamboo Substances 0.000 title claims abstract description 32
- 238000004821 distillation Methods 0.000 title claims description 9
- 238000000197 pyrolysis Methods 0.000 claims abstract description 62
- 238000003763 carbonization Methods 0.000 claims abstract description 28
- 238000003860 storage Methods 0.000 claims abstract description 12
- 238000005485 electric heating Methods 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000011521 glass Substances 0.000 claims description 4
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000009776 industrial production Methods 0.000 abstract description 4
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 230000003285 pharmacodynamic effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 14
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 10
- 239000007788 liquid Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000009413 insulation Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000002398 materia medica Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 208000023504 respiratory system disease Diseases 0.000 description 1
- 230000010415 tropism Effects 0.000 description 1
- 230000002792 vascular Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses fresh bamboo draining and distilling equipment, which comprises a dry distillation tank, a condenser, a pipeline filter, a cooler, a control cabinet and a storage tank, wherein the dry distillation tank is of a horizontal structure, an electric heating sleeve is arranged on a tank body of the dry distillation tank, a track is arranged in the dry distillation tank, a tank cover is arranged on one side of the dry distillation tank, a fan assembly is arranged on the other side of the dry distillation tank, a distilling outlet, a fixed supporting leg and a lifting supporting leg are arranged at the bottom of the dry distillation tank, the distilling outlet is connected with an inlet of the cooler through a valve b, the outlet of the cooler is divided into two paths, one path is communicated with the atmosphere after passing through a valve e, and the other path is connected with the storage tank after passing through a valve d; the top of the carbonization tank is provided with a steam inlet and an exhaust port, the exhaust port is connected with the inlet of the condenser after passing through the pressure release valve, the outlet of the condenser is divided into two paths, one path is communicated with the atmosphere after passing through the valve c, and the other path is connected with the inlet of the cooler after passing through the valve a and the pipeline filter. The dry distillation product has the advantages of high content of pharmacodynamic characteristic components, high total yield, energy conservation, environmental protection and low investment cost, and is suitable for large-scale industrial production.
Description
Technical Field
The utility model relates to the technical field of carbonization equipment, in particular to fresh bamboo draining and distilling equipment.
Background
The succus Bambusae is yellowish clear liquid juice of bamboo stalk which flows out after being baked with fire. It is also called "Sheng Ji Zhi Sheng also" by Ben Cao Jing Ji Zhi (materia Medica of the present utility model). Nineteen classical works on the herb property, meridian tropism and clinical application of the herb are well documented. The traditional dry distillation method of bamboo juice recorded in Ben Cao gang mu is mainly divided into two types: a firing method and a carbonization method. At present, thirteen compound Chinese patent medicines containing bamboo juice are widely used for respiratory diseases.
The equipment for extracting the fresh bamboo juice by the water boiling method is generally a multifunctional extraction tank, so that industrial production can be formed. However, the fresh bamboo juice produced by the water boiling method has low content of limited components, is easy to mold and deteriorate, the product quality can not meet the requirements of baking and dry distillation, and the process method is completely inconsistent with the requirements of the traditional fresh bamboo draining and distilling process. The traditional fire-baking method is in accordance with the traditional dry distillation method of fresh bamboo juice in technology, but the method has the disadvantages of serious bamboo material waste, low yield, low efficiency, environmental pollution and the like, and is difficult to realize high-efficiency industrial production.
In the prior art, a carbonization device is also used for extracting fresh bamboo juice, for example, the publication number is CN115634469A, and the name is: the utility model provides a negative pressure dry distillation box and extraction method of fresh bamboo juice is drawed to negative pressure, includes the dry distillation box body, negative pressure fan and vapor generator, and the dry distillation box body outer wall is equipped with the heat preservation, and negative pressure fan and vapor generator set up outside the dry distillation box body, and dry distillation box body bottom is equipped with electric heating pipe 102, and dry distillation box body top is equipped with the air nozzle, and vapor generator communicates the air nozzle through first connecting pipe, and negative pressure fan communicates the dry distillation box body through the second connecting pipe. By adopting the structure, steam is introduced in the carbonization stage, and the water molecules in the bamboo chips or organic components in the vascular bundles are steamed out under the action of high temperature by utilizing the humidity difference principle; when the temperature in the tank is further increased to reach the carbonization temperature, the negative pressure fan is started to pump the interior of the carbonization tank to negative pressure, so that the carbonization of fresh bamboo juice can be accelerated in a negative pressure vacuum environment, the yield is improved, the resource consumption is low, and the production cost is further reduced. However, the heating assembly of the dry distillation tank is only arranged at the bottom of the device, and bamboo chips are easy to cause uneven heating in the dry distillation tank, so that important active ingredients in bamboo cannot be fully extracted, and the bamboo is heated unevenly, so that the quality uniformity of dry distillation liquid is poor.
Disclosure of Invention
The utility model aims to overcome the defects of the prior art, adapt to the actual needs and provide fresh bamboo draining and distilling equipment.
In order to achieve the aim of the utility model, the utility model adopts the following technical scheme:
the fresh bamboo draining and distilling device comprises a dry distillation tank, a condenser, a pipeline filter, a cooler, a control cabinet and a storage tank, wherein the dry distillation tank is of a horizontal structure, an electric heating sleeve is wrapped on the tank body of the dry distillation tank, a track for bearing a carrier is arranged at the inner bottom of the dry distillation tank, a tank cover is arranged at one side of the dry distillation tank, a fan assembly is arranged at the other side of the dry distillation tank, the fan assembly comprises a motor and fan blades, the fan blades are arranged in the dry distillation tank, and the motor is arranged outside the dry distillation tank;
the bottom of the carbonization tank is provided with a distillation outlet and fixed supporting feet on one side close to the fan assembly, the bottom of the carbonization tank is provided with lifting supporting feet on one side close to the tank cover, the distillation outlet is connected with an inlet of a cooler after passing through a valve b5, the outlet of the cooler is divided into two paths, one path is communicated with the atmosphere after passing through a valve e10, and the other path is connected with a storage tank after passing through a valve d 8;
the top of the dry distillation tank is provided with a steam inlet near one side of the tank cover, one side of the top of the dry distillation tank near the fan assembly is provided with an exhaust port, the exhaust port is connected with the inlet of the condenser after passing through the pressure release valve, the outlet of the condenser is divided into two paths, one path is communicated with the atmosphere after passing through the valve c6, and the other path is connected with the inlet of the cooler after passing through the valve a3 and the pipeline filter.
Further, a guide cover is arranged outside the fan blade in the dry distillation tank, and the guide cover is in a horn shape with the outer diameter gradually reduced along the airflow direction.
Further, the electric heating sleeve comprises a heating pipe which surrounds the retort body and a heat preservation layer which covers the outer part of the heating pipe.
Further, a sight glass is arranged on the tank cover.
Further, a safety valve and a pressure transmitter are arranged at the exhaust port, and a temperature transmitter is arranged on the carbonization tank.
The utility model has the beneficial effects that:
1. the carbonization tank adopts a horizontal structure, a track for bearing a carrier is arranged at the inner bottom of the carbonization tank, and the inclination angle of the carbonization tank is adjustable, so that materials can be conveniently fed in and discharged out; adopt cyclic annular parcel's heating method, simultaneously, inside fan and the kuppe of having set up of retort can make retort inside heated medium circulate in accumulational bamboo periphery and center effectively, improve the homogeneity of dry flow temperature, make and draw more abundant to carbonization efficiency and quality have been improved.
2. Before carbonization, steam is utilized to preheat, and air is exhausted by controlling corresponding valves during preheating, so that the heating speed and steam heating efficiency of bamboo are improved, and after preheating, liquid water in a tank is exhausted by controlling corresponding valves, so that subsequent carbonization is facilitated, and oxidation reaction of distillate during subsequent carbonization is avoided.
3. When the pressure of the steam exceeds the set pressure during carbonization, the pressure release valve can be automatically opened to release pressure, the steam carrying the effective components can enter the cooler after passing through the filter and enter the storage tank after being cooled by the cooler, so that the loss of the effective components can be prevented, and the extraction rate of the effective components is improved.
4. The dry distillation product has the advantages of high content of pharmacodynamic characteristic components, high total yield, simple structure, energy conservation, environmental protection and low investment cost, and is very suitable for large-scale industrial production.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
in the figure: 1. dry distillation tank, 2, condenser, 3, valve a, 4, pipe filter, 5, valve b, 6, valve c, 7, cooler, 8, valve d, 9, control cabinet, 10, valve e, 11, storage tank, 101, steam inlet, 102, heating pipe, 103, exhaust 103, 104, pressure transmitter, 105, pressure relief valve, 106, safety valve, 107, temperature transmitter, 108, fan assembly, 109, pod, 110, distillation outlet, 111, insulation, 112, lifting support, 113, track, 114, carrier, 115, sight glass.
Description of the embodiments
The utility model may be further described by the following examples, however, the scope of the utility model is not limited to the following examples: it is to be understood that the embodiments described herein are disclosed by way of illustration only and that the utility model is not intended to be limited in scope to the details of construction and the arrangement of components set forth in the following description or illustrated in the drawings. Furthermore, in describing the preferred embodiments, specific terminology will be resorted to for the sake of clarity. It is to be understood that each specific term includes all technical equivalents that operate in a similar manner to accomplish a similar purpose.
The utility model takes the quality of traditional baking and dry distillation as a reference, improves the uniformity of the quality of the dry distillation liquid and the sufficiency of extraction while increasing the productivity, adopts 2000L type dry distillation equipment corresponding to the utility model to produce the same products as the traditional baking method, can produce 50kg per day by the traditional baking line, can produce 200kg per day by the dry distillation equipment, has the transit waiting time of less than 10 minutes in continuous operation, reduces the number of personnel to below 2, and improves the production efficiency by 300 percent.
Example 1: referring to fig. 1, the fresh bamboo draining and distilling device of the present utility model comprises a dry distillation tank 1, a condenser 2, a pipeline filter 4, a cooler 7, a control cabinet 9 and a storage tank 11, wherein the dry distillation tank 1 is of a horizontal structure, an electric heating jacket is wrapped on the tank body of the dry distillation tank 1, a track 113 for carrying a carrier 114 is arranged at the inner bottom of the dry distillation tank 1, the carrier 114 can be used for loading bamboo, a tank cover is arranged at one side of the dry distillation tank 1, the carrier 114 can be conveniently moved in and out by opening the tank cover, a fan assembly 108 is arranged at the other side of the dry distillation tank 1, the fan assembly 108 comprises a motor and fan blades, wherein the fan blades are arranged in the dry distillation tank 1, the motor is arranged outside the dry distillation tank 1, and the fan is started to enable medium inside the dry distillation tank to circulate, thereby being helpful for uniform heating of bamboo;
the bottom of the carbonization tank 1 is provided with a distillation outlet 110 and fixed supporting feet on one side close to the fan assembly 108, and a lifting supporting foot 112 is arranged on one side close to the tank cover of the bottom of the carbonization tank 1, namely, the inclination angle of the carbonization tank 1 can be adjusted as required, so that the tank body can be kept horizontal when materials enter and exit, and when carbonization works, a certain inclination is kept, so that carbonization liquid can conveniently flow out of the tank body, and the inside is prevented from being heated for a long time, thereby improving carbonization efficiency and quality;
the distillation outlet 110 is connected with the inlet of a cooler 7 after passing through a valve b5, the cooler 7 is used for cooling distillate, the outlet of the cooler 7 is divided into two paths, one path passes through a valve e10 and then is communicated with the atmosphere, and the other path passes through a valve d8 and then is connected with a storage tank 11;
the top of the dry distillation tank 1 is provided with a steam inlet 101 near one side of the tank cover, the top of the dry distillation tank 1 is provided with an exhaust port 103 near one side of the fan assembly 108, the exhaust port 103 is connected with the inlet of the condenser 2 after passing through a pressure release valve 105, the outlet of the condenser 2 is divided into two paths, one path is communicated with the atmosphere after passing through a valve c6, and the other path is connected with the inlet of the cooler 7 after passing through a valve a3 and a pipeline filter 4.
In this embodiment, the outside that is located the fan blade in retort 1 is equipped with kuppe 109, and kuppe 109 is the horn-shaped that the external diameter reduces gradually along the air current direction, can play the effect of flow direction through setting up kuppe 109, and when the fan blade rotated, the air current passed through kuppe 109, can make the air current concentrate rapidly, plays the effect of reinforcing wind-force, and the air current of being convenient for gets into in the carrier 114, carries out the circulation and the diffusion of hot air flow from inside outwards, makes the bamboo in the carrier 114 be heated more evenly.
In this embodiment, the electric heating jacket includes a heating pipe 102 surrounding the retort 1 and a heat insulation layer 111 covering the outside of the heating pipe 102, where the heat insulation layer 111 can perform a heat insulation function to reduce heat loss.
In this embodiment, in order to facilitate observation of the internal state of the retort, a sight glass 115 is provided on the lid.
In this embodiment, the exhaust port 103 is provided with a safety valve 106 and a pressure transmitter 104, the retort 1 is provided with a temperature transmitter 107, the pressure transmitter 104 is used for monitoring the pressure in the retort, the temperature transmitter 107 is used for monitoring the temperature in the retort, and the pressure transmitter 104 and the temperature transmitter 107 are respectively connected with the control cabinet 9 through wires.
Example 2, fresh bamboo juice dry distillation, specifically comprises the following steps:
(1) Breaking bamboo into suitable size and loading in the carrier 114, opening the cover to push the carrier into the retort 1 along the track 113, and closing the cover;
(2) Preheating, namely keeping the valve b5 and the valve e10 open, introducing steam from the steam inlet 101, keeping other valves closed, when steam exists at the outlet of the valve e10, closing the valve b5 and the valve e10, continuously introducing steam into the carbonization tank, keeping the internal pressure at 0.05-0.2 MPa, keeping for 10-30 min, closing the steam after the time, opening the valve b5 and the valve e10, and closing the valve b5 and the valve e10 after the liquid water in the tank is exhausted; when preheating starts, the valve b5 and the valve e10 are kept open, so that when steam is introduced into the tank, an outlet for exhausting internal air is reserved for the tank body, when the steam is generated at the opening of the valve e10, the air in the tank is considered to be exhausted, at the moment, the valve b5 and the valve e10 are closed, and the steam is continuously introduced to heat the bamboo, and as the specific heat of the air is far lower than that of the steam, the heating efficiency of the steam can be greatly improved by exhausting the air, so that the bamboo is heated in a short time, and the production efficiency is improved;
(3) Dry distillation, namely, opening the electric heating pipe 102, the fan assembly 108, the valve a3 and the valve d8, keeping the internal temperature at 160-180 ℃, setting the pressure at 0.5-0.7 MPa, and keeping the internal temperature for 0.5-3 h;
in the holding process, when the steam pressure exceeds the set pressure, the pressure release valve 105 is automatically opened to release pressure, the steam carrying the effective components enters the cooler 7 after passing through the filter 4 and enters the storage tank 11 after being cooled by the cooler 7, and the design can prevent the effective components from being lost, so that the extraction rate of the effective components is improved;
closing the valve a3 after the holding time is up, and opening the pressure release valve 105 and the valve c6 to release the pressure in the tank to the atmospheric pressure;
valve b5 is opened and the distillate is cooled by cooler 7 and then enters storage tank 11.
While the fundamental and principal features of the utility model and advantages of the utility model have been shown and described, it will be apparent to those skilled in the art that the utility model is not limited to the details of the foregoing exemplary embodiments, but may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present disclosure describes embodiments, not every embodiment is provided with a separate embodiment, and that this description is provided for clarity only, and that the disclosure is not limited to the embodiments described in detail below, and that the embodiments described in the examples may be combined as appropriate to form other embodiments that will be apparent to those skilled in the art.
Claims (5)
1. Fresh bamboo draining and distilling equipment comprises a dry distillation tank (1), a condenser (2), a pipeline filter (4), a cooler (7), a control cabinet (9) and a storage tank (11), and is characterized in that the dry distillation tank (1) is of a horizontal structure, an electric heating sleeve is wrapped on a tank body of the dry distillation tank (1), a track (113) for bearing a carrier (114) is arranged at the inner bottom of the dry distillation tank (1), a tank cover is arranged at one side of the dry distillation tank (1), a fan assembly (108) is arranged at the other side of the dry distillation tank, the fan assembly (108) comprises a motor and fan blades, the fan blades are arranged in the dry distillation tank (1), and the motor is arranged outside the dry distillation tank (1);
a distillation outlet (110) and fixed supporting feet are arranged on one side, close to a fan assembly (108), of the bottom of the carbonization tank (1), a lifting supporting foot (112) is arranged on one side, close to a tank cover, of the bottom of the carbonization tank (1), the distillation outlet (110) is connected with an inlet of a cooler (7) through a valve b (5), the outlet of the cooler (7) is divided into two paths, one path is communicated with the atmosphere after passing through a valve e (10), and the other path is connected with a storage tank (11) after passing through a valve d (8);
one side that the top of retort (1) is close to the cover is equipped with steam inlet (101), and one side that the top of retort (1) is close to fan subassembly (108) is equipped with gas vent (103), gas vent (103) are connected with the entry of condenser (2) behind relief valve (105), and the export of condenser (2) divides two ways, communicates with each other with the atmosphere after passing through valve c (6) one way, and the other way is connected with the entry of cooler (7) behind valve a (3) and pipeline filter (4).
2. The dry distillation apparatus as claimed in claim 1, wherein a guide shell (109) is arranged in the dry distillation tank (1) outside the fan blades, and the guide shell (109) has a horn shape with an outer diameter gradually decreasing along the air flow direction.
3. The retorting apparatus as claimed in claim 1, characterized in that said electric heating jacket comprises a heating tube (102) surrounding the body of the retort (1) and an insulating layer (111) covering the outside of the heating tube (102).
4. Destructive distillation apparatus according to claim 1, wherein the lid is provided with a sight glass (115).
5. The retorting apparatus as claimed in claim 1, wherein a safety valve (106) and a pressure transmitter (104) are provided at the exhaust port (103), and a temperature transmitter (107) is provided on the retorting tank (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321587708.2U CN219907483U (en) | 2023-06-21 | 2023-06-21 | Fresh bamboo draining distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321587708.2U CN219907483U (en) | 2023-06-21 | 2023-06-21 | Fresh bamboo draining distillation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219907483U true CN219907483U (en) | 2023-10-27 |
Family
ID=88467704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321587708.2U Active CN219907483U (en) | 2023-06-21 | 2023-06-21 | Fresh bamboo draining distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219907483U (en) |
-
2023
- 2023-06-21 CN CN202321587708.2U patent/CN219907483U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11505764B2 (en) | Continuous distillation process | |
| CN107987866A (en) | A kind of device and method of the efficient depolymerization co-producing bio-oil of solid waste microwave and charcoal | |
| CN107192224B (en) | The energy-efficient drying device of minute-pressure self arrangement timber and drying means | |
| CN206544996U (en) | A kind of equipment for producing fresh bamboo sap | |
| CN219907483U (en) | Fresh bamboo draining distillation equipment | |
| CN114350392A (en) | Method for extracting fresh bamboo juice by uniformly dry distilling bamboo chips | |
| CN214390089U (en) | A dry distillation device for producing bright bamboo juice | |
| CN116554907A (en) | Fresh bamboo draining distillation equipment and process thereof | |
| CN205641936U (en) | Fodder drying -machine waste heat recovery utilizes system | |
| CN110470105A (en) | A kind of timber flash baking equipment and furnace drying method | |
| CN207642286U (en) | A kind of efficient sendust powder under vacuum coating unit | |
| JP2023508931A (en) | Organic liquid purification and recovery apparatus and methods | |
| CN219079587U (en) | Copper-aluminum composite annealing furnace | |
| CN212864716U (en) | Selenium wine distillation equipment | |
| CN107671552B (en) | Aluminium sheet circle production line and its construction technology | |
| CN201095634Y (en) | Pure grain dry material wine brewing device | |
| CN206424938U (en) | A kind of energy-efficient chemical reaction kettle | |
| CN115746889A (en) | Method and device for preparing combustible gas by biomass baking and polypropylene co-pyrolysis | |
| CN106867828A (en) | A kind of Quick production method of Chinese chestnut wine | |
| CN204798416U (en) | Quick sterilization apparatus of mushroom wood flour | |
| CN210974612U (en) | Small-size intelligent equipment that draws | |
| CN208635531U (en) | A kind of transformation method drying equipment hot blast flow guide structure | |
| CN207811678U (en) | A kind of device of solid waste microwave efficient depolymerization co-producing bio-oil and charcoal | |
| CN206587760U (en) | A kind of composite fibre preparation system | |
| CN206924444U (en) | A kind of energy-conserving and environment-protective medicine enrichment facility |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240603 Address after: 333302 Lei Gongshan, ShuangTian Town, Leping City, Jingdezhen City, Jiangxi Province Patentee after: JIANGXI JINGDE CHINESE MEDICINE CO.,LTD. Country or region after: China Address before: No. 1688 Meiling Avenue, Wanli District, Nanchang City, Jiangxi Province Patentee before: JIANGXI University OF TRADITIONAL CHINESE MEDICINE Country or region before: China |
|
| TR01 | Transfer of patent right |