CN104534845A - Continuous vacuum belt type drying device - Google Patents
Continuous vacuum belt type drying device Download PDFInfo
- Publication number
- CN104534845A CN104534845A CN201410797346.9A CN201410797346A CN104534845A CN 104534845 A CN104534845 A CN 104534845A CN 201410797346 A CN201410797346 A CN 201410797346A CN 104534845 A CN104534845 A CN 104534845A
- Authority
- CN
- China
- Prior art keywords
- conveyer belt
- drying device
- continuous vacuum
- seal casinghousing
- heating
- 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
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a continuous vacuum belt type drying device, and belongs to the technical field of drying. The continuous vacuum belt type drying device comprises a sealing shell (1), at least one conveying belt (2) arranged in the sealing shell (1) in the front-and-back direction, a raw material tank (3) arranged at the upper portion of the front portion of the conveying belt (2), a smashing collecting structure (6) arranged at the lower portion of the back portion of the conveying belt (2), a swing feeding structure (4) arranged at the front portion of the sealing shell (1), a discharging structure (5) arranged at the back portion of the sealing shell (1), a vacuum structure (10) connected with the sealing shell (1), at least one heating structure (8) arranged in the mode of being tightly close to the front portion of the conveying belt (2) and at least one cooling structure (9) arranged in the mode of being tightly close to the back portion of the conveying belt (2). The swing feeding structure (4) is connected with an output pipe of the raw material tank (3), the discharging structure (5) is located at the upper back portion adjacent to the back portion of the conveying belt (2), and the smashing collecting structure (6) is located under the discharging structure (5).
Description
Technical field
The present invention relates to technical field of drying, particularly a kind of continuous vacuum belt drying device, particularly relates to a kind of drying device for dry yeast extract.
Background technology
YE (yeast extract) adopts with the food yeast of rich in protein as raw material, adopt self-dissolving, enzymolysis, separation, the modern biotechnology new and high technology such as concentrated, refiningly after protein in yeast cells, nucleic acid etc. are carried out degraded to form, a kind of brown color solubility paste or slight yellow powdery natural product.Main component is polypeptide, amino acid, flavour nucleotide, B family vitamin and trace element.
YE (yeast extract) adopts with the food yeast of rich in protein as raw material according to the regulation of Pharmacopoea Chinensis, adopt self-dissolving, enzymolysis, separation, the modern biotechnology new and high technology such as concentrated, refiningly after protein in yeast cells, nucleic acid etc. are carried out degraded to form, a kind of brown color solubility paste or slight yellow powdery natural product.Main component is polypeptide, amino acid, flavour nucleotide, B family vitamin and trace element.Be a kind of excellent natural flavouring, in food service industry, tool has been widely used.Also be the primary raw material in ideal biological culture medium raw material and fermentation industry.Yeast extract is yeast by after utilizing self complete self-dissolving of hydrolase system after plasmolysis, removes the product after cell membrane and insoluble molecule.In production process, the strict hydrolysis degree controlling yeast oneself protein matter meets different application needs; Finally by yeast extract simmer down to half paste, creamy product, the powdered product of oil embedding, microcapsules and microparticle is to be applicable to different application needs.But in the production process of yeast extract, have a very difficult problem to be exactly the drying of enzymolysis product, its particle had is little, the feature that stickiness is large, result in its and is very easy to blocking.
The spray-dired method of current industrial main employing, spray-dired principle be by air after filtration and heating, enter drier headspace distributor, hot-air enters hothouse in the shape of a spiral equably.Feed liquid is through the high speed centrifugal atomization device at tower body top, and (rotation) sprays into imperceptible vaporific liquid pearl, and contact with hot-air flow within the extremely short time drying to be finished product.Finished product exports by bottom drying tower He in cyclone separator continuously, and waste gas is emptying by air-introduced machine.
Spray-dired feature is that rate of drying is fast, and feed liquid is amassed through atomization rear surface to be increased greatly, in hot-air flow, just can evaporate the moisture content of 95%-98% instantaneously, complete and only need the several seconds drying time, be specially adapted to the drying of heat sensitive material.Product has the good uniformity, mobility and dissolubility, and product purity is high, and quality is good.Production process simplifies, the features such as convenient operation and control.But same shortcoming is also clearly:
1. equipment is more complicated, and floor space is large, and once investment is large;
2. atomizer, powder recovering device price is higher;
3. need air capacity many, increase the power consumption of air blast and the capacity of retracting device;
4. the thermal efficiency is not high, and heat loss is large.
5. spray-dired volume dry tenacity is little, therefore its hothouse volume is very large.
6. can there is product and glue wall situation.
Freeze drying also known as lyophilization, be by wet stock or solution at a lower temperature (-10 ~-50 DEG C) be frozen into solid-state, the dry run of then under high vacuum, wherein moisture being dewatered without liquid state is directly sublimed into gaseous state.But equally there is shortcoming:
1. operating temperature is low, and dried material keeps original chemical composition and physical property
2. spraying dry energy ezpenditure is large, and drying medium consumption is many, and Btu utilization is uneconomical.
3. heat exhaustion is fewer than other drying means.
Summary of the invention
In order to solve the problem, the invention provides a kind of continuous vacuum belt drying device for dry yeast extract.Described technical scheme is as follows:
Embodiments provide a kind of continuous vacuum belt drying device, this device comprises seal casinghousing 1, be located at least one conveyer belt 2 in seal casinghousing 1 along the longitudinal direction, be located at the head tank 3 of conveyer belt 2 front upper, be located at the pulverizing collection structure 6 of conveyer belt 2 lower rear, be located at the swing feeding structure 4 of seal casinghousing 1 front portion, be located at the discharging structure 5 at seal casinghousing 1 rear portion, the vacuum structure 10 be connected with seal casinghousing 1, be close at least one heating arrangement 8 that conveyer belt 2 front portion is arranged and at least one cooling structure 9 being close to the setting of conveyer belt 2 rear portion, described swing feeding structure 4 is connected with the output channel of head tank 3, described discharging structure 5 is positioned at adjacent back upper place, conveyer belt 2 rear portion, described pulverizing collection structure 6 is positioned at immediately below described discharging structure 5.
Further, the drying unit that the embodiment of the present invention provides also comprises temperature control system, described temperature control system comprises multiple sensor and control unit, each heating arrangement 8 correspondence arranges at least one temperature sensor, each cooling structure 9 correspondence arranges at least one temperature sensor, described sensor is electrically connected with control unit, and described control unit is electrically connected with heating arrangement 8 and cooling structure 9.
Wherein, heating arrangement 8 in the embodiment of the present invention comprises heating plate 11, heater 12, control valve 13, circulating pump 14 and replenisher tank 15, setting below conveyer belt 2 is close to by described heating plate 11, described heating plate 11 forms closed circuit with replenisher tank 15 by pipeline, described pipeline is provided with heater 12, control valve 13 and circulating pump 14, and described heater 12 and control valve 13 are electrically connected with control unit.
Particularly, conveyer belt 2 front portion in the embodiment of the present invention has been arranged side by side 3 heating arrangements, 8,3 heating arrangements 8 from front to back and has shared a replenisher tank 15, and described conveyer belt 2 rear portion is provided with a cooling structure 9.
Further, the seal casinghousing 1 that the embodiment of the present invention provides is provided with multiple visual window 16.
Further, the drying unit that the embodiment of the present invention provides also comprises purging system, and described purging system comprises collects water tank and multiple spray head, and described spray head is located at directly over conveyer belt 2, and described collection water tank is connected by pipeline with bottom seal casinghousing 1.
Further, the oven dry that the embodiment of the present invention provides is stated device and is also comprised speed control system, and described speed control system is electrically connected with the drive motors of conveyer belt 2.
Wherein, the pulverizing collection structure 6 in the embodiment of the present invention comprises pulverizing structure 17, the first valve discharge bucket 7, collecting tank 18 and the second valve discharge bucket 19 that set gradually from top to bottom.
The beneficial effect of the continuous vacuum belt drying device that the embodiment of the present invention provides is:
1, conveyer belt can control its running status and the speed of service respectively.
2, the feed pump on head tank can control its running status and charging rate respectively.
3, swing the cloth motor cloth angle on feeding structure, the speed of service can step-less adjustment.
4, temperature controls to adopt control valve and digital sensing control technology thus the heating-up temperature temperature-constant operation ensureing every section.
5, heating system adopts superheated water to be the heat form of medium.Also the multiple heating modes such as Steam Heating, vacuum belt drier heat-conducting oil heating and the heating of direct-type electric boiling plate can be provided according to the requirement of client.
6, equipment is furnished with the full-automatic incumbent firms system of CIP, and sanitary cleaning is quick and convenient.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme in the embodiment of the present invention, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the continuous vacuum belt drying device that the embodiment of the present invention provides.
In figure: 1 seal casinghousing, 2 conveyer belts, 3 head tanks, 4 swing feeding structure, 5 discharging structures, 6 pulverize collection structure, 7 first valve discharge buckets, 8 heating arrangements, 9 cooling structures, 10 vacuum structures, 11 heating plates, 12 heaters, 13 control valves, 14 circulating pumps, 15 replenisher tanks, 16 visual windows, 17 pulverize structure, 18 collecting tanks, 19 second valve discharge buckets.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearly, below in conjunction with accompanying drawing, embodiment of the present invention is described further in detail.
See Fig. 1, embodiments provide a kind of continuous vacuum belt drying device, this device comprises seal casinghousing 1, be located at least one conveyer belt 2 in seal casinghousing 1 along the longitudinal direction, be located at the head tank 3 of conveyer belt 2 front upper, be located at the pulverizing collection structure 6 of conveyer belt 2 lower rear, be located at the swing feeding structure 4 of seal casinghousing 1 front portion, be located at the discharging structure 5 at seal casinghousing 1 rear portion, the vacuum structure 10 be connected with seal casinghousing 1, be close at least one heating arrangement 8 that conveyer belt 2 front portion is arranged and at least one cooling structure 9 etc. being close to the setting of conveyer belt 2 rear portion.Wherein, seal casinghousing 1 is Cylindrical housing structure, and its rear and front end is hinged with openable capping.Wherein, heating arrangement 8 and cooling structure 9 adopt contact design to be respectively used to carry out heating and cooling to the material on conveyer belt 2.Wherein, vacuum structure 10, for ensureing that seal casinghousing 1 inside is in vacuum state, is specifically as follows multi-stage roots Water-ring vacuum pump assembly.Wherein, swing feeding structure 4 to be connected for raw material uniform spreading is spread across conveyer belt with the output channel of head tank 3.Discharging structure 5 be arranged in adjacent back upper place, conveyer belt 2 rear portion for will caking dried feed stripping and slicing and send into and pulverize collection structure 6, can be specifically that the hand hay cutter moved up and down breaks device.Pulverize collection structure 6 to be positioned at immediately below discharging structure 5 for pulverizing collection dried feed.
Wherein, head tank 3 and swing feeding structure 4 are located at seal casinghousing 1 front upper part, and discharging structure 5 is located at seal casinghousing 1 upper back, pulverize collection structure 6 and are positioned at seal casinghousing 1 rear lower.
Further, the drying unit that the embodiment of the present invention provides also comprises temperature control system for controlling the temperature of drying course, this temperature control system comprises multiple sensor and control unit, each heating arrangement 8 correspondence arranges at least one temperature sensor, and each cooling structure 9 correspondence arranges at least one temperature sensor.Particularly, the corresponding drying section of each heating arrangement 8, the corresponding cooling section of each cooling structure 9, the inwall of the seal casinghousing 1 of each section arranges a temperature sensor for detecting the temperature of each section.Wherein, sensor is electrically connected with control unit, and control unit is electrically connected with heating arrangement 8 and cooling structure 9 and controls separately it.
Wherein, see Fig. 1, the heating arrangement 8 in the embodiment of the present invention adopts hot water heating mode, can certainly adopt other modes, is the common technique of this area, and the present embodiment omits to be described in detail.Particularly, heating arrangement 8 comprises heating plate 11, heater 12, control valve 13, circulating pump 14 and replenisher tank 15 etc.Wherein, setting below conveyer belt 2 is close to by heating plate 11, and heating plate 11 and replenisher tank 15 form closed circuit by pipeline.This pipeline is provided with heater 12, control valve 13 and circulating pump 14, and heater 12 and control valve 13 are electrically connected for controlling heating-up temperature with control unit.Wherein, circulating pump 14 and replenisher tank 15 can be located at outside seal casinghousing 1.
Wherein, the cooling structure 9 in the embodiment of the present invention adopts cold water cooling mode, comprises the cold plate being close to setting below conveyer belt 2, and cold plate is provided with a circulation line, and this circulation line is connected with refrigeration structure.
Particularly, see Fig. 1, conveyer belt 2 front portion in the embodiment of the present invention has been arranged side by side 3 heating arrangements, 8,3 heating arrangements 8 from front to back and has shared a replenisher tank 15, and conveyer belt 2 rear portion is provided with a cooling structure 9.Certainly also other modes can be adopted as required.
Further, see Fig. 1, the seal casinghousing 1 that the embodiment of the present invention provides is provided with multiple visual window 16 for observing oven-dried condition.Particularly, visual window 16 can be set in seal casinghousing 1 rear and front end.
Further, the drying unit that the embodiment of the present invention provides also comprises purging system, this purging system comprises collects water tank and multiple spray head, spray head is located at directly over conveyer belt 2 and is connected with water supply installation, collects water tank and is connected for collecting foreign material and water for cleaning by pipeline with bottom seal casinghousing 1.
Further, the oven dry that the embodiment of the present invention provides is stated device and is also comprised speed control system for controlling the speed of conveyer belt 2, and this speed control system is electrically connected with the drive motors of conveyer belt 2.
Further, the drying unit that the embodiment of the present invention provides also comprises deviation-rectifying system, and this deviation-rectifying system is located at conveyer belt 2, and material strip departs from center when running and is not more than ± 0.5cm to adopt closed-loop control to ensure.
Wherein, see Fig. 1, the pulverizing collection structure 6 in the embodiment of the present invention comprises the air-tightness for ensureing whole device such as pulverizing structure 17, first valve discharge bucket 7, collecting tank 18 and the second valve discharge bucket 19 set gradually from top to bottom.
Wherein, the output channel (can be flexible pipe) of the head tank 3 in the embodiment of the present invention is provided with by-pass valve control for controlling material loading speed.
Wherein, swing feeding structure 4 in the embodiment of the present invention comprises reducing motor and fork, and this reducing motor is fixed on seal casinghousing 1, and its rotating shaft is vertically arranged, one end of fork is fixed in rotating shaft in the horizontal direction, and the other end is connected with the output channel of head tank 3.
Below in conjunction with Fig. 1, this device is described: this device is a kind of continuous feed, the contact vacuum dryer of continuous discharge form, feed liquid to be dried directly enters the dryer inner being in high vacuum by conveying mechanism, on some dry zones material paved in drying machine by swing feeding structure 4, special rubber roll is driven to drive dry zone to move along drying device cylindrical shell direction with the speed of setting by motor, three separate heating plates and a coldplate is all provided with below every bar dry zone, dry zone and heating plate, coldplate fits tightly, in the mode of transmission of heat by contact by the energy transferring required for drying to material.When dry zone moves to the other end from one end of cylindrical shell, material drying through supercooling, when dry zone turns back, dried material cake is peeled off from dry zone, the discharging structure 5 moved up and down by one, hit down and pulverize in collection structure, the material after pulverizing is by the discharge bucket discharging of two air-lock formulas.Because material directly enters through after a while progressively dry (normally 30-60 minute) under condition of high vacuum degree, after dry, the particle of gained has crystallization effect to a certain degree, has micropore from microstructure inside simultaneously.After being directly crushed to required particle diameter, the mobility of particle is fine, can direct tablet compressing or encapsulating capsule, and simultaneously because particle has the open structure of microcosmic, instant capacity is fabulous.And the outward appearance of particle is good, for instant (electuary) product, can the class of improving product greatly.Band-type vacuum drier is respectively at two ends continuous feed, the continuous discharge of fuselage.
This device is respectively at two ends continuous feed, the continuous discharge of fuselage, and batching and output section can be arranged in clean room, and whole dry run is completely closed, does not contact with external environment, meets the requirement of GMP.Directly concentrated extract can be sent into this device to carry out drying and need not add any auxiliary material, the dose of final products can be reduced like this, improve the class of product.Product, in whole dry run, is in vacuum, enclosed environment, dry run gentleness (product temperature 40-135 DEG C), for the extraction of natural plants, can keep its color to greatest extent, obtain high-quality final products.Vacuum crawler continuous drier can carry out CIP incumbent firms completely, criticizing and criticize, can changing easily between product and product, reduces labour intensity, reduces process procedure, ensure that product quality.
The above the specific embodiment of the present invention, does not form limiting the scope of the present invention.Various other that any technical conceive according to the present invention is made change and distortion accordingly, all should be included in the protection domain of the claims in the present invention.
Claims (8)
1. a continuous vacuum belt drying device, it is characterized in that, comprise seal casinghousing (1), be located at least one conveyer belt (2) in seal casinghousing (1) along the longitudinal direction, be located at the head tank (3) of conveyer belt (2) front upper, be located at the pulverizing collection structure (6) of conveyer belt (2) lower rear, be located at the swing feeding structure (4) that seal casinghousing (1) is anterior, be located at the discharging structure (5) at seal casinghousing (1) rear portion, the vacuum structure (10) be connected with seal casinghousing (1), be close at least one heating arrangement (8) that conveyer belt (2) front portion is arranged and at least one cooling structure (9) being close to the setting of conveyer belt (2) rear portion, described swing feeding structure (4) is connected with the output channel of head tank (3), described discharging structure (5) is positioned at adjacent back upper place, conveyer belt (2) rear portion, described pulverizing collection structure (6) is positioned at immediately below described discharging structure (5).
2. continuous vacuum belt drying device according to claim 1, it is characterized in that, described device also comprises temperature control system, described temperature control system comprises multiple sensor and control unit, each heating arrangement (8) correspondence arranges at least one temperature sensor, each cooling structure (9) correspondence arranges at least one temperature sensor, described sensor is electrically connected with control unit, and described control unit is electrically connected with heating arrangement (8) and cooling structure (9).
3. continuous vacuum belt drying device according to claim 2, it is characterized in that, described heating arrangement (8) comprises heating plate (11), heater (12), control valve (13), circulating pump (14) and replenisher tank (15), described heating plate (11) is close to conveyer belt (2) below and is arranged, described heating plate (11) and replenisher tank (15) form closed circuit by pipeline, described pipeline is provided with heater (12), control valve (13) and circulating pump (14), described heater (12) and control valve (13) are electrically connected with control unit.
4. continuous vacuum belt drying device according to claim 3, it is characterized in that, described conveyer belt (2) front portion has been arranged side by side 3 heating arrangements (8) from front to back, 3 heating arrangements (8) share a replenisher tank (15), and described conveyer belt (2) rear portion is provided with a cooling structure (9).
5. continuous vacuum belt drying device according to claim 1, is characterized in that, described seal casinghousing (1) is provided with multiple visual window (16).
6. continuous vacuum belt drying device according to claim 1, it is characterized in that, described device also comprises purging system, described purging system comprises collects water tank and multiple spray head, described spray head is located at directly over conveyer belt (2), and described collection water tank is connected by pipeline with seal casinghousing (1) bottom.
7. continuous vacuum belt drying device according to claim 1, it is characterized in that, described device also comprises speed control system, and described speed control system is electrically connected with the drive motors of conveyer belt (2).
8. continuous vacuum belt drying device according to claim 1, it is characterized in that, described pulverizing collection structure (6) comprises the pulverizing structure (17), the first valve discharge bucket (7), collecting tank (18) and the second valve discharge bucket (19) that set gradually from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410797346.9A CN104534845A (en) | 2014-12-19 | 2014-12-19 | Continuous vacuum belt type drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410797346.9A CN104534845A (en) | 2014-12-19 | 2014-12-19 | Continuous vacuum belt type drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104534845A true CN104534845A (en) | 2015-04-22 |
Family
ID=52850419
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410797346.9A Pending CN104534845A (en) | 2014-12-19 | 2014-12-19 | Continuous vacuum belt type drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104534845A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105352299A (en) * | 2015-12-07 | 2016-02-24 | 江苏知原药业有限公司 | Medicine vacuum dryer |
| CN106047704A (en) * | 2016-06-01 | 2016-10-26 | 厦门鹭港兆康生物科技有限公司 | Production line for culturing plant stem cells on large scale |
| CN107356081A (en) * | 2017-04-19 | 2017-11-17 | 浙江温兄机械阀业有限公司 | A kind of vacuum belt drier |
| CN109282597A (en) * | 2018-11-01 | 2019-01-29 | 南京仁恒轴承滚动体有限公司 | A kind of needle roller drying device |
| CN112539637A (en) * | 2020-12-11 | 2021-03-23 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
| CN114249610A (en) * | 2021-12-30 | 2022-03-29 | 瓮福达州化工有限责任公司 | Preparation process and device of ammonium potassium polyphosphate containing chelated medium and trace elements |
| CN114485124A (en) * | 2022-02-18 | 2022-05-13 | 重庆衡生药用胶囊有限公司 | Infrared drying method for hollow capsules |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5366055A (en) * | 1976-11-26 | 1978-06-13 | Kimura Shoten Kk | Automatic vacuum dryer |
| CN1854657A (en) * | 2005-04-28 | 2006-11-01 | 上海华琪实业有限公司 | Automatic continuous-band freezing drier at vacuum low temperature |
| CN101368788A (en) * | 2007-08-14 | 2009-02-18 | 温州市金榜轻工机械有限公司 | Vacuum belt type drying units |
| CN201876067U (en) * | 2010-11-23 | 2011-06-22 | 浙江温兄机械阀业有限公司 | Vacuum belt-type dryer |
| CN202719847U (en) * | 2012-06-15 | 2013-02-06 | 浙江远力健药业有限责任公司 | Crawler type vacuum drying equipment |
| CN204313619U (en) * | 2014-12-19 | 2015-05-06 | 山东圣琪生物有限公司 | A kind of continuous vacuum belt drying device |
-
2014
- 2014-12-19 CN CN201410797346.9A patent/CN104534845A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5366055A (en) * | 1976-11-26 | 1978-06-13 | Kimura Shoten Kk | Automatic vacuum dryer |
| CN1854657A (en) * | 2005-04-28 | 2006-11-01 | 上海华琪实业有限公司 | Automatic continuous-band freezing drier at vacuum low temperature |
| CN101368788A (en) * | 2007-08-14 | 2009-02-18 | 温州市金榜轻工机械有限公司 | Vacuum belt type drying units |
| CN201876067U (en) * | 2010-11-23 | 2011-06-22 | 浙江温兄机械阀业有限公司 | Vacuum belt-type dryer |
| CN202719847U (en) * | 2012-06-15 | 2013-02-06 | 浙江远力健药业有限责任公司 | Crawler type vacuum drying equipment |
| CN204313619U (en) * | 2014-12-19 | 2015-05-06 | 山东圣琪生物有限公司 | A kind of continuous vacuum belt drying device |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105352299A (en) * | 2015-12-07 | 2016-02-24 | 江苏知原药业有限公司 | Medicine vacuum dryer |
| CN106047704A (en) * | 2016-06-01 | 2016-10-26 | 厦门鹭港兆康生物科技有限公司 | Production line for culturing plant stem cells on large scale |
| CN106047704B (en) * | 2016-06-01 | 2018-05-29 | 厦门鹭港兆康生物科技有限公司 | A kind of production line of pilot scale culture plant stem cell |
| CN107356081A (en) * | 2017-04-19 | 2017-11-17 | 浙江温兄机械阀业有限公司 | A kind of vacuum belt drier |
| CN107356081B (en) * | 2017-04-19 | 2019-11-12 | 浙江温兄机械阀业有限公司 | A kind of vacuum belt drier |
| CN109282597A (en) * | 2018-11-01 | 2019-01-29 | 南京仁恒轴承滚动体有限公司 | A kind of needle roller drying device |
| CN112539637A (en) * | 2020-12-11 | 2021-03-23 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
| CN112539637B (en) * | 2020-12-11 | 2022-06-21 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
| CN114249610A (en) * | 2021-12-30 | 2022-03-29 | 瓮福达州化工有限责任公司 | Preparation process and device of ammonium potassium polyphosphate containing chelated medium and trace elements |
| CN114485124A (en) * | 2022-02-18 | 2022-05-13 | 重庆衡生药用胶囊有限公司 | Infrared drying method for hollow capsules |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104534845A (en) | Continuous vacuum belt type drying device | |
| CN105258480B (en) | A kind of high-efficiency and continuous vacuum microwave drier | |
| CN101368788A (en) | Vacuum belt type drying units | |
| CN108497526A (en) | For normal pressure ultrasonic atomizatio-spouted drying device of low frequency microwave pulse of conditioning fruit-vegetable and its application | |
| CN204313619U (en) | A kind of continuous vacuum belt drying device | |
| CN102878788B (en) | A kind of heat sensitive material vacuum disk continuous drier | |
| CN108130272A (en) | Black garlic fermentation drying machine | |
| CN207562368U (en) | The dry machine of vacuum spraying band | |
| CN203443286U (en) | Continuous production type freeze dryer | |
| CN204293890U (en) | Spray dryer | |
| CN210663704U (en) | Rotary vacuum drying machine for producing perfluoroalkyl xanthyl fluoride derivatives | |
| CN103335500B (en) | A kind of continuous seepage type freeze dryer | |
| CN205279670U (en) | Vacuum drying apparatus | |
| CN101919443B (en) | Absorption type low-temperature drying tower | |
| CN104896877A (en) | Ultrasonic atomizing and pulse microwave vacuum drying device for liquid material and drying method | |
| CN204268814U (en) | A kind of Novel vacuum drying device | |
| CN205228104U (en) | Maize seed processing lines | |
| CN209263542U (en) | A kind of double-cone vacuum dryer | |
| CN203908230U (en) | Hot-shaft stirring type continuous vacuum drying device | |
| CN207197166U (en) | Electric heating rotary dryer | |
| CN102764515A (en) | Drying method and drying device of anionic surfactant | |
| CN204930206U (en) | A kind of concentrator for milk powder producing | |
| CN207622453U (en) | The mechanism closed and rotary dryer are automatically turned on for feeding chamber intermittence | |
| CN201729773U (en) | Vacuum drying device for polycarboxylic acid water-reducing agent | |
| CN206803650U (en) | With the electric heating rotary dryer for automatically turning on closing organ |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150422 |