CN106546067B - Low-temperature integrated drying method for replacing bacterial cellulose gel film - Google Patents

Low-temperature integrated drying method for replacing bacterial cellulose gel film Download PDF

Info

Publication number
CN106546067B
CN106546067B CN201510596535.4A CN201510596535A CN106546067B CN 106546067 B CN106546067 B CN 106546067B CN 201510596535 A CN201510596535 A CN 201510596535A CN 106546067 B CN106546067 B CN 106546067B
Authority
CN
China
Prior art keywords
displacing agent
drying
tank
drying tank
storage tank
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
Application number
CN201510596535.4A
Other languages
Chinese (zh)
Other versions
CN106546067A (en
Inventor
钟春燕
钟宇光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hainan Yeguo Foods Co Ltd
Original Assignee
Hainan Yeguo Foods Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hainan Yeguo Foods Co Ltd filed Critical Hainan Yeguo Foods Co Ltd
Priority to CN201510596535.4A priority Critical patent/CN106546067B/en
Publication of CN106546067A publication Critical patent/CN106546067A/en
Application granted granted Critical
Publication of CN106546067B publication Critical patent/CN106546067B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The invention provides a method for performing replacement and low-temperature integrated drying on a bacterial cellulose gel film, which mainly comprises the following steps: the device comprises a drying tank (1) and a displacing agent storage tank (2), wherein an air outlet (3) with a valve is arranged at the upper part of the drying tank (1), a water outlet (4) with a valve and a displacing agent inlet (5) are arranged at the lower part of the drying tank (1), an electric heating device (6) and a removable middle shaft lever (7) are arranged at the middle shaft of the drying tank; the upper part of the displacing agent storage tank (2) is provided with a displacing agent recovery inlet (8), the lower part of the displacing agent storage tank (2) is provided with a displacing agent outlet (9), the air outlet (3) with a valve at the upper part of the drying tank (1) is connected with the displacing agent recovery inlet (8) at the upper part of the displacing agent storage tank (2) through a conduit, and the displacing agent inlet (5) at the lower part of the drying tank (1) is connected with the displacing agent outlet (9) at the lower part of the displacing agent storage tank (2) through a conduit.

Description

Low-temperature integrated drying method for replacing bacterial cellulose gel film
Technical Field
The invention relates to a material drying system and method, in particular to a bacterial cellulose gel film replacement low-temperature integrated drying system and method.
Background
Bacterial cellulose is a biomaterial synthesized by metabolism of some microorganisms, which has a similar basic structure as natural cellulose, but has many unique properties, for example, excellent mechanical properties, high biocompatibility, good biodegradability, etc., since it does not contain lignin, hemicellulose, etc. associated products, and has a crystallinity as high as 95% or more and a high degree of polymerization as high as 2000-8000. It has wide application prospect in a plurality of technical fields. At present, bacterial cellulose is mainly subjected to static fermentation culture by a liquid culture medium to obtain a bacterial cellulose gel film with very high water content. However, in an increasing number of applications, it is desirable to use dry bacterial cellulose films that are substantially free of water. The conventional drying methods mainly comprise hot air drying, freeze drying and the like, but the high temperature and freezing inevitably affect the spatial network structure of the bacterial cellulose, so that many physical and chemical characteristics of the bacterial cellulose membrane, such as porosity, mechanical properties, conductivity and the like, are affected. The supercritical drying technology which has been developed in recent years can maintain the space network structure of the bacterial cellulose to the maximum extent, but the cost is high, the requirement on equipment is high, and the technology is still in a laboratory stage and cannot be applied industrially on a large scale.
Disclosure of Invention
The invention provides a system and a method for performing replacement and low-temperature integrated drying on a bacterial cellulose gel film, which mainly comprise the following steps: the device comprises a drying tank, a displacing agent storage tank, an electric heating device and a water outlet, wherein the upper part of the drying tank is provided with an air outlet with a valve, the lower part of the drying tank is provided with a water outlet with a valve, a displacing agent inlet and a detachable middle shaft rod, and the middle shaft of the drying tank is provided with the electric heating device; the upper part of the displacing agent storage tank is provided with a displacing agent recovery inlet, the lower part of the displacing agent storage tank is provided with a displacing agent outlet, the air outlet with a valve at the upper part of the drying tank is connected with the displacing agent recovery inlet at the upper part of the displacing agent storage tank through a conduit, and the displacing agent inlet at the lower part of the drying tank is connected with the displacing agent outlet at the lower part of the displacing agent storage tank through a conduit.
In the system, the side wall of the drying tank 1 is also provided with a transparent observation window for observing the position of the liquid level. Preferably it extends to the bottom of the drying tank.
In the system, the electric heating device is controlled by the temperature sensor and the temperature control device, and the temperature sensor measures the temperature in the drying tank to control whether the heating device is started.
In the system, an air outlet with a valve at the upper part of the drying tank is connected with a displacing agent recycling inlet at the upper part of the displacing agent storage tank through a condenser and a conduit.
In the system, a displacer inlet at the lower part of the drying tank is connected with a displacer outlet at the lower part of the displacer storage tank through a pump and a conduit. The pump is reversible.
According to the replacement low-temperature integrated drying system and method provided by the invention, the water in the bacterial cellulose gel film can be replaced by the replacement agent through the replacement drying technology, and then the replacement agent is removed from the bacterial cellulose film through the low-temperature drying technology. The replacement drying is completely carried out at normal temperature, and the low-temperature drying is only carried out at 50-60 ℃ according to the type of the replacement agent, so that the damage of high temperature or freezing to the space network structure of the bacterial cellulose membrane can be avoided, and various performances of the dried bacterial cellulose membrane can be improved. In addition, the replacement low-temperature drying system and the replacement low-temperature drying method provided by the invention can also enable replacement drying and low-temperature drying to be integrally carried out in the same tank body, do not need a plurality of devices, transfer bacterial cellulose materials for a plurality of times, can also recycle a replacement agent, are low in cost and simple to operate, and have good application prospects.
Drawings
The drawings are only for purposes of illustrating and explaining the present invention and are not to be construed as limiting the scope of the present invention. Wherein:
FIG. 1 is a schematic structural diagram of an embodiment of the present invention.
In the figure:
1-drying in a tank; 2-a displacer storage tank; 3-an air outlet with a valve; 4-water outlet with valve; 5-a displacer inlet; 6-an electric heating device; 7-a central shaft; 8-a displacer recovery inlet; 9-a displacer outlet; 10-a transparent viewing window; 11-a temperature sensor; 12-temperature control means; 13-a condenser; 14-Pump.
Detailed Description
The invention is further elucidated below with reference to the drawing. In the following detailed description, the invention is described by way of illustration only, and not by way of limitation. Those skilled in the art will be able to modify the detailed description to follow in various ways without departing from the spirit and scope of the invention, and it is intended to be within the scope of the invention.
As shown in figure 1, the system and the method for replacing low-temperature integrated drying of the bacterial cellulose gel film comprise a drying tank 1 and a displacer storage tank 2, wherein an air outlet 3 with a valve is arranged at the upper part of the drying tank 1, a water outlet 4 with a valve and a displacer inlet 5 are arranged at the lower part of the drying tank 1, and an electric heating device 6 is arranged, the electric heating device 6 is controlled by a temperature sensor 11 and a temperature control device 12, and the temperature sensor 11 measures the temperature in the drying tank 1 to control whether the heating device 6 is started. A removable middle shaft lever 7 is arranged at the middle shaft of the drying tank, and after the removable middle shaft lever is removed, the bacterial cellulose gel film containing water is wound on the middle shaft lever and then is installed back into the drying tank; the upper part of the displacer storage tank 2 is provided with a displacer recovery inlet 8, the lower part of the displacer storage tank 2 is provided with a displacer outlet 9, the air outlet 3 with a valve at the upper part of the drying tank 1 is connected with the displacer recovery inlet 8 at the upper part of the displacer storage tank 2 through a condenser 13, and the displacer inlet 5 at the lower part of the drying tank 1 is connected with the displacer outlet 9 at the lower part of the displacer storage tank 2 through a pump 14. The side wall of the drying tank 1 is also provided with a transparent observation window 10 extending to the bottom of the drying tank for observing the position of the liquid level.
The replacement low-temperature integrated drying system and the method have the working modes as follows:
firstly, taking down a central shaft 7 in a drying tank 1, winding a water-containing bacterial cellulose gel film on the central shaft 7, then installing the central shaft back into the drying tank 1, closing an air outlet 3 at the upper part of the drying tank and a water outlet 4 at the lower part of the drying tank, opening a displacing agent inlet 5, then pumping a displacing agent in a displacing agent storage tank 2 into the drying tank 1 through a pump 14 until the liquid level of the displacing agent in the drying tank is higher than that of the bacterial cellulose gel film roll (observing the liquid level through a transparent observation window), stopping pumping the displacing agent, closing the displacing agent inlet 5, and standing for solvent displacement drying. The displacing agent enters the bacterial cellulose gel film to displace the water in the bacterial cellulose gel film, and the displacing agent is lighter than water, so that the liquid in the drying tank can be layered, the lower layer is water, and the upper layer is the displacing agent. After the displacement drying is finished, a water outlet 4 at the lower part of the drying tank 1 is opened to discharge wastewater, after the wastewater is discharged (the discharged liquid can be observed to contain a displacing agent or observe the liquid level change through a transparent observation window), the water outlet 4 is closed, a displacing agent inlet 5 is opened, the remaining displacing agent in the drying tank is pumped into a displacing agent storage tank 2, and the displacing agent inlet 5 is closed after the completion. And opening an air outlet 3 at the upper part of the drying tank, starting the electric heating device, controlling the temperature in the drying tank to be slightly higher than the boiling point of the displacing agent through a temperature sensor and a temperature control device, evaporating the displacing agent from the air outlet 3 in a changed gas state, condensing the gas through a condenser 13, and refluxing the gas into a displacing agent storage tank 2.

Claims (7)

1. A method for replacing and drying bacterial cellulose gel film at low temperature is characterized in that: a replacement low-temperature integrated drying system is adopted for drying, the replacement low-temperature integrated drying system is composed of a drying tank (1) and a displacing agent storage tank (2), an air outlet (3) with a valve is arranged at the upper part of the drying tank (1), a water outlet (4) with a valve and a displacing agent inlet (5) are arranged at the lower part of the drying tank (1), an electric heating device (6) is arranged, and a removable middle shaft rod (7) is arranged at the middle shaft of the drying tank; a displacing agent recovery inlet (8) is formed in the upper part of the displacing agent storage tank (2), a displacing agent outlet (9) is formed in the lower part of the displacing agent storage tank (2), an air outlet (3) with a valve in the upper part of the drying tank (1) is connected with the displacing agent recovery inlet (8) in the upper part of the displacing agent storage tank (2) through a guide pipe, and a displacing agent inlet (5) in the lower part of the drying tank (1) is connected with the displacing agent outlet (9) in the lower part of the displacing agent storage tank (2) through a guide pipe; the drying method comprises the following steps: firstly, taking down a middle shaft rod (7) in a drying tank (1), winding a water-containing bacterial cellulose gel film on the middle shaft rod (7), then installing the middle shaft rod back into the drying tank (1), sealing an air outlet (3) at the upper part and a water outlet (4) at the lower part of the drying tank, opening a displacer inlet (5), then pumping a displacer in a displacer storage tank (2) into the drying tank (1), stopping pumping the displacer and closing the displacer inlet (5) when the liquid level of the displacer in the drying tank is higher than that of the bacterial cellulose gel film roll, and standing for solvent displacement drying; after the displacement drying is finished, opening a water outlet (4) at the lower part of the drying tank (1) to discharge wastewater, closing the water outlet (4) after the wastewater is discharged, opening a displacing agent inlet (5), pumping the residual displacing agent in the drying tank into a displacing agent storage tank (2), and closing the displacing agent inlet (5) after the completion of the displacement drying; and opening the air outlet (3) at the upper part of the drying tank, starting the electric heating device (6), controlling the temperature in the drying tank to be slightly higher than the boiling point of the displacing agent, evaporating the displacing agent from the air outlet (3) to be changed into gas, condensing, and refluxing to the displacing agent storage tank (2).
2. The bacterial cellulose gel film displacement low-temperature drying method according to claim 1, characterized in that: the side wall of the drying tank (1) is also provided with a transparent observation window (10) through which the liquid level of the displacing agent is observed.
3. The bacterial cellulose gel film displacement low-temperature drying method according to claim 2, characterized in that: the transparent viewing window (10) extends to the bottom of the drying tank.
4. The bacterial cellulose gel film displacement cryodrying method according to any one of claims 1 to 3, characterized in that: the electric heating device (6) is controlled by a temperature sensor (11) and a temperature control device (12).
5. The bacterial cellulose gel film displacement cryodrying method according to any one of claims 1 to 3, characterized in that: an air outlet (3) with a valve at the upper part of the drying tank (1) is connected with a displacing agent recovery inlet (8) at the upper part of the displacing agent storage tank (2) through a condenser (13) and a conduit, and the displacing agent is evaporated, condensed through the condenser (13) and then refluxed into the displacing agent storage tank (2).
6. The bacterial cellulose gel film displacement low-temperature drying method according to claim 5, characterized in that: the displacer inlet (5) at the lower part of the drying tank (1) is connected with the displacer outlet (9) at the lower part of the displacer storage tank (2) through a pump (14) and a conduit.
7. The bacterial cellulose gel film displacement low-temperature drying method according to claim 6, characterized in that: the pump (14) is reversible.
CN201510596535.4A 2015-09-18 2015-09-18 Low-temperature integrated drying method for replacing bacterial cellulose gel film Active CN106546067B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510596535.4A CN106546067B (en) 2015-09-18 2015-09-18 Low-temperature integrated drying method for replacing bacterial cellulose gel film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510596535.4A CN106546067B (en) 2015-09-18 2015-09-18 Low-temperature integrated drying method for replacing bacterial cellulose gel film

Publications (2)

Publication Number Publication Date
CN106546067A CN106546067A (en) 2017-03-29
CN106546067B true CN106546067B (en) 2022-08-19

Family

ID=58361729

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510596535.4A Active CN106546067B (en) 2015-09-18 2015-09-18 Low-temperature integrated drying method for replacing bacterial cellulose gel film

Country Status (1)

Country Link
CN (1) CN106546067B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107930543B (en) * 2017-12-28 2023-08-11 乐山职业技术学院 Device and method for solvent replacement and normal-pressure drying for preparing aerogel

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1201354A (en) * 1967-11-20 1970-08-05 Blaw Knox Co Removing solvent from free flowing material
US3653983A (en) * 1968-11-22 1972-04-04 Henkel & Cie Gmbh Compositions for displacing water adhering to metal surfaces and process
GB2038653A (en) * 1978-12-27 1980-07-30 Kloeckner Humboldt Deutz Ag Dressing Slurries
EP0194589A2 (en) * 1985-03-11 1986-09-17 AlliedSignal Inc. Apparatus and method for cleaning and drying surfaces of non-absorbent articles
US5458786A (en) * 1994-04-18 1995-10-17 The Center For Innovative Technology Method for dewatering fine coal
JP2000070605A (en) * 1998-09-04 2000-03-07 Du Pont Mitsui Fluorochem Co Ltd Method and apparatus for draining/washing
JP2004249250A (en) * 2003-02-21 2004-09-09 Denso Corp Draining and drying device
CN1658937A (en) * 2002-06-03 2005-08-24 财团法人电力中央研究所 Method for removing water contained in solid using liquid material
CN101121666A (en) * 2006-08-11 2008-02-13 小仓合成工业株式会社 Process for producing amino compound
CN101168467A (en) * 2007-09-28 2008-04-30 天津大学 Sludge replacing and dewatering method and device
CN101398254A (en) * 2007-09-30 2009-04-01 浙江医药股份有限公司新昌制药厂 Peptide-containing antibiotic finished product drying method
CN101603772A (en) * 2009-06-11 2009-12-16 山东省科学院生物研究所 A kind of product drying and solvent recovery process and equipment
CN101666575A (en) * 2008-09-03 2010-03-10 淄博矿业集团有限责任公司 Drying process and drying system for material containing low-boiling point, inflammable and explosive organic solvent
CN102040512A (en) * 2009-10-13 2011-05-04 中国石油化工股份有限公司 Crude terephthalic acid mother solution replacing method
JP2011255353A (en) * 2010-06-11 2011-12-22 Asahi Glass Co Ltd Draining/drying method and draining/drying system
CN103272539A (en) * 2013-05-07 2013-09-04 李光武 Method and device for preparing aerogel by drying under reduced pressure
WO2013183007A1 (en) * 2012-06-07 2013-12-12 Kemira Oyj High solids content microfibrillated cellulose and manufacturing thereof

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB797605A (en) * 1955-07-25 1958-07-02 Patenthandels A G Apparatus for drying fibres
GB1054373A (en) * 1963-05-17
US3386181A (en) * 1966-11-15 1968-06-04 Du Pont Method of removing water and apparatus therefor
US3559297A (en) * 1969-03-10 1971-02-02 Allied Chem Process and apparatus for removing water from solid surfaces
US3589023A (en) * 1969-06-10 1971-06-29 Allied Chem Process and apparatus for removing water from solid surfaces at low temperatures
FR2146657A5 (en) * 1971-07-22 1973-03-02 Jeumont Schneider
CN1064075C (en) * 1994-10-28 2001-04-04 奥林帕斯光学工业株式会社 Composition and method for washing and drying
TW440572B (en) * 1996-04-11 2001-06-16 Mitsui Petrochemical Ind Method of drying solid polymer and drying apparatus
CN1303881A (en) * 2000-01-07 2001-07-18 四川大学 Divided-flow solvent-removing and product-drying method for producing polyvinyl alcohol pellet
CA2614606C (en) * 2005-07-13 2008-10-28 Bitmin Resources Inc. Oil sand processing apparatus
JP2008034779A (en) * 2006-06-27 2008-02-14 Dainippon Screen Mfg Co Ltd Method and equipment for processing substrate
CN100501921C (en) * 2006-06-27 2009-06-17 大日本网目版制造株式会社 Substrate processing method and substrate processing apparatus
CA2629593A1 (en) * 2008-04-11 2009-10-11 James Michael Dunbar Feedback control scheme for optimizing dewatering processes
CN101433562B (en) * 2008-12-17 2011-09-07 中国林业科学研究院林产化学工业研究所 Method for preparing ginkgo leaf extract powder using supercritical liquid desiccation and device thereof
CN101780390B (en) * 2009-01-16 2012-11-21 中国科学院过程工程研究所 Substitution and dehydration method for water contained solid materials and device
CN102108001A (en) * 2009-12-24 2011-06-29 大连理工大学 Film pressure thermal dehydration method and equipment for high-moisture sludge
JP5298041B2 (en) * 2010-02-03 2013-09-25 株式会社カワタ Drying apparatus and inert gas replacement method
US20120047764A1 (en) * 2010-08-24 2012-03-01 David Campion System and method for drying substrates
US8815050B2 (en) * 2011-03-22 2014-08-26 Marathon Gtf Technology, Ltd. Processes and systems for drying liquid bromine
KR101433851B1 (en) * 2012-05-11 2014-08-26 김병훈 Solvent for the Preparation of Aerogel and Method for Preparing Hydrophobic Aerogel by Using the Same
JP6455962B2 (en) * 2013-03-18 2019-01-23 芝浦メカトロニクス株式会社 Substrate processing apparatus and substrate processing method
CN104019639A (en) * 2014-06-07 2014-09-03 张家港市进润彩印包装有限公司 Solvent recoverable vacuum drying process
CN204017442U (en) * 2014-08-26 2014-12-17 浙江圣达生物药业股份有限公司 A kind of solvent separation unit
TWM512208U (en) * 2015-01-16 2015-11-11 Grand Plastic Technology Corp Processing equipment integrating moisture removal and drying
CN205102512U (en) * 2015-09-18 2016-03-23 海南椰国食品有限公司 Bacteria cellulose gel mould replacement low temperature integral type drying system

Patent Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1201354A (en) * 1967-11-20 1970-08-05 Blaw Knox Co Removing solvent from free flowing material
US3653983A (en) * 1968-11-22 1972-04-04 Henkel & Cie Gmbh Compositions for displacing water adhering to metal surfaces and process
GB2038653A (en) * 1978-12-27 1980-07-30 Kloeckner Humboldt Deutz Ag Dressing Slurries
EP0194589A2 (en) * 1985-03-11 1986-09-17 AlliedSignal Inc. Apparatus and method for cleaning and drying surfaces of non-absorbent articles
US5458786A (en) * 1994-04-18 1995-10-17 The Center For Innovative Technology Method for dewatering fine coal
JP2000070605A (en) * 1998-09-04 2000-03-07 Du Pont Mitsui Fluorochem Co Ltd Method and apparatus for draining/washing
CN1658937A (en) * 2002-06-03 2005-08-24 财团法人电力中央研究所 Method for removing water contained in solid using liquid material
JP2004249250A (en) * 2003-02-21 2004-09-09 Denso Corp Draining and drying device
CN101121666A (en) * 2006-08-11 2008-02-13 小仓合成工业株式会社 Process for producing amino compound
CN101168467A (en) * 2007-09-28 2008-04-30 天津大学 Sludge replacing and dewatering method and device
CN101398254A (en) * 2007-09-30 2009-04-01 浙江医药股份有限公司新昌制药厂 Peptide-containing antibiotic finished product drying method
CN101666575A (en) * 2008-09-03 2010-03-10 淄博矿业集团有限责任公司 Drying process and drying system for material containing low-boiling point, inflammable and explosive organic solvent
CN101603772A (en) * 2009-06-11 2009-12-16 山东省科学院生物研究所 A kind of product drying and solvent recovery process and equipment
CN102040512A (en) * 2009-10-13 2011-05-04 中国石油化工股份有限公司 Crude terephthalic acid mother solution replacing method
JP2011255353A (en) * 2010-06-11 2011-12-22 Asahi Glass Co Ltd Draining/drying method and draining/drying system
WO2013183007A1 (en) * 2012-06-07 2013-12-12 Kemira Oyj High solids content microfibrillated cellulose and manufacturing thereof
CN103272539A (en) * 2013-05-07 2013-09-04 李光武 Method and device for preparing aerogel by drying under reduced pressure

Also Published As

Publication number Publication date
CN106546067A (en) 2017-03-29

Similar Documents

Publication Publication Date Title
CN106546067B (en) Low-temperature integrated drying method for replacing bacterial cellulose gel film
CN104525282A (en) Novel constant temperature and moisture test box
CN105879720A (en) Preparation method of heat and chemical cross-linked hyperbranched polysiloxane pervaporation membrane
CN106759634A (en) A kind of outdoor non-negative pressure water-supply installation with antifreeze function
KR101613948B1 (en) Laver to recycle heat drying equipment included in the dry heat cycle heat pump-type device and method using the same heat of dry air and latent heat recovery method
CN205618328U (en) A combination equipment for preparing it is dry, clean gaseous
CN207356607U (en) Vacuum distillation apparatus and decompression distillation system
CN206240102U (en) A kind of de- list experimental provision of polymer emulsion
CN205102512U (en) Bacteria cellulose gel mould replacement low temperature integral type drying system
EP2864721A1 (en) Heat exchanger facility
CN102654350B (en) Method for starting oxygen making unit
CN104457050B (en) Centrifugal refrierator in a kind of rotating boosting
CN205736064U (en) Ultrathin capacitor thin film sided corona treatment attemperating unit
CN204235771U (en) For the efficient crosslinking apparatus of PAP
CN206778005U (en) A kind of dehydration of organic solvent device
JP5682925B2 (en) Underground heat storage type air conditioner
CN206787189U (en) Liquaemin low-temperature vacuum drying case
CN207049597U (en) A kind of double film biogas cabinet condensate winterization systems
CN206566907U (en) A kind of circulating energy-saving device of polymer stabilizer production equipment
CN106334329B (en) A kind of de- single experimental provision of polymer emulsion
CN203994119U (en) Redwood vacuum drying casting all-in-one with dry condensate water device
CN110715541A (en) High-temperature agricultural product drying equipment and method based on supercritical carbon dioxide energy storage
CN205528790U (en) Utilize device of living beings continuous fermentation preparation hydrogen
JP2015221007A (en) Algae oil extraction method and algae oil extraction apparatus
JP5860563B1 (en) Complex liquid separation and purification equipment

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant