CN109304058A - A kind of oxalic acid bioengineering separation equipment - Google Patents

A kind of oxalic acid bioengineering separation equipment Download PDF

Info

Publication number
CN109304058A
CN109304058A CN201811060769.7A CN201811060769A CN109304058A CN 109304058 A CN109304058 A CN 109304058A CN 201811060769 A CN201811060769 A CN 201811060769A CN 109304058 A CN109304058 A CN 109304058A
Authority
CN
China
Prior art keywords
plate
oxalic acid
deflector
web plate
separation
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.)
Granted
Application number
CN201811060769.7A
Other languages
Chinese (zh)
Other versions
CN109304058B (en
Inventor
范应元
范诺
范一诺
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.)
Weifang Medical University
Original Assignee
Weifang Medical University
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 Weifang Medical University filed Critical Weifang Medical University
Priority to CN201811060769.7A priority Critical patent/CN109304058B/en
Publication of CN109304058A publication Critical patent/CN109304058A/en
Application granted granted Critical
Publication of CN109304058B publication Critical patent/CN109304058B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D36/00Filter circuits or combinations of filters with other separating devices

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Centrifugal Separators (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

The invention discloses a kind of oxalic acid bioengineering separation equipments, including body, the inside upper part of the body is equipped with deflector, the upside space of deflector is initial gross separation chamber, separating plate is provided on the upside of deflector, carrying web plate is provided on the inside of separating plate, the centre of separating plate is equipped with central axis, the bottom of body is additionally provided with the driving motor with center axis connection, the downside of deflector is in being equipped with secondary separation web plate on central axis, the downside of secondary separation web plate is in being mounted with storing plate on body inner wall, the space that storing plate and body are constituted is storage cavity.Structure of the invention is compact, and space occupied is small, and the oxalic acid particle gone out by secondary separation is less containing waste liquid, and regular shape, and processing quality is good, high-efficient, promotes the performance of enterprises, is conducive to investment application.

Description

A kind of oxalic acid bioengineering separation equipment
Technical field
The present invention relates to oxalic acid production technology applied technical field, specifically a kind of oxalic acid bioengineering separation equipment.
Background technique
The production of whole world oxalic acid is concentrated mainly on Asia, and 33% is used for pharmaceutical industry;25% is used for rare-earth trade;35% For intermetallic composite coating and aluminium product industry;Remaining is 7% for the industries such as oxalate, dyestuff intermediate.With oxalic acid application field Extension, especially the quantity of pesticide and medicine intermediate oxalate is increasing, and produces vanillic aldehyde new process with glyoxalic acid Development, the demand of oxalic acid will sustainedly and stably increase.
Purification oxalic acid is that recrystallization is purified and produced on the basis of industrial goods oxalic acid, with the increasing to oxalic acid demand Add, people require to be increasingly stringenter to purification oxalic acid technique.In the production of purification oxalic acid, stable product quality is controllable, scene Good controllable and consumption of raw materials the control of environment is to refine the key link of oxalic acid production.Currently, oxalate product quality is not Stablize, especially when carrying out Crystallization Separation, existing separation equipment space occupied is big, and separated structure is single, the grass after separation Granulates are more containing waste liquid, and regular shape is poor, and processing quality is poor, low efficiency, influence the performance of enterprises.
Therefore, currently practical to overcome there is an urgent need to develop a kind of oxalic acid bioengineering separation equipment for the above status Deficiency in meets the needs of oxalic acid production and processing.
Summary of the invention
The purpose of the present invention is to provide a kind of oxalic acid bioengineering separation equipments, to solve to propose in above-mentioned background technique The problem of.
To achieve the above object, the invention provides the following technical scheme:
A kind of oxalic acid bioengineering separation equipment, including body, the body are enclosed cylindrical tube structure, machine The bottom outer ring of body is provided with more supporting legs, and the inside upper part of the body is equipped with deflector, the upside space of deflector For initial gross separation chamber, it is provided with separating plate on the upside of the deflector, carrying web plate is provided on the inside of the separating plate, it is described The centre of separating plate is equipped with central axis, and the lower end of central axis is stretched out from the bottom of body, the sealed bottom of central axis and body Rotation connection, the bottom of the body are additionally provided with the driving motor with center axis connection, and the downside of the deflector is in central axis On secondary separation web plate is installed, the downside of secondary separation web plate is in being mounted with storing plate, the storage on body inner wall The space that flitch and body are constituted is storage cavity, offers several discard solution discharge ports on the central axis, discard solution discharge port passes through The channel opened up in central axis is connected to the space in separating plate.
As a further solution of the present invention: the deflector be up big and down small pyramidal structure cylinder, deflector it is upper It holds and is smoothly connected with the inner sidewall parabola of body.
As a further solution of the present invention: the separating plate is pyramidal structure, and separating plate is arranged in parallel with deflector, Vertical range between separating plate and deflector is 10-20cm, and the upper end diameter of separating plate is the 1/2 of body internal diameter.
As a further solution of the present invention: the carrying web plate is reticular structure made of stainless steel material, bearer network Plate is middle part arc concave configuration, and the inner wall parabola of the outer ring and separating plate that carry web plate is smoothly connected.
As a further solution of the present invention: the outer diameter of the central axis is the 1/2 of deflector lower end diameter.
As a further solution of the present invention: the secondary separation web plate is the pyramidal structure that outer ring tilts down setting, Secondary separation web plate is reticular structure made of stainless steel material, and the mesh of the mesh of secondary separation web plate and carrying web plate is big Small shape is identical.
As a further solution of the present invention: the diameter of the secondary separation web plate is less than the internal diameter of body.
As a further solution of the present invention: the storing plate includes the cylindrical tube on top and the conically shaped of lower part Body, the outer diameter of cylindrical tube are less than the diameter of secondary separation web plate, and the lower end of conical shell and the inner sidewall connection of body are solid It is fixed.
As a further solution of the present invention: the discard solution discharge port is located at the downside of storing plate upper surface.
As a further solution of the present invention: the top center of the body is also equipped with feed pipe, the lower end of feed pipe Vertical range with carrying web plate is 10-20cm, and the upper end of feed pipe is equipped with hopper, and the bottom of the body, which is additionally provided with, to be used for The sewer pipe that waste liquid is discharged in body is circumferentially with multiple drainage conduits being connected to storage cavity bottom on the side wall of the body.
Compared with prior art, the beneficial effects of the present invention are: the oxalic acid bioengineering separation equipment, crystallisation by cooling is filled The substance set is added in hopper, rear to be dropped on carrying web plate by feed pipe, and waste liquid can be filtered out by carrying web plate, and By the discard solution discharge port outflow on central axis, center axis rotation is driven by driving motor, and then separating plate rotates, and may make The substance centrifuge separation on web plate is carried, the oxalic acid particle isolated can fall on deflector, by the structure setting of deflector, Be slipped on secondary separation web plate conducive to oxalic acid particle, by secondary separation web plate can secondary separation go out it is useless in oxalic acid particle Liquid, rear oxalic acid particle can be dropped into storage cavity and be collected, the waste liquid of discard solution discharge port discharge and secondary from secondary separation web plate The waste liquid filtered out can be collected by the bottom space of body;Whole device is compact-sized, and space occupied is small, goes out by secondary separation Oxalic acid particle it is less containing waste liquid, and regular shape, processing quality is good, high-efficient, promotes the performance of enterprises, is conducive to investment application.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the overlooking structure diagram of separating plate part in the present invention.
Fig. 3 be Fig. 1 in A-A to structural schematic diagram.
In figure: 1- sewer pipe, 2- driving motor, 3- supporting leg, 4- discard solution discharge port, 5- central axis, 6- deflector, 7- are held Support grid plate, 8- feed pipe, 9- hopper, 10- separating plate, 11- initial gross separation chamber, 12- body, 13- secondary separation web plate, 14- storage Expect chamber, 15- storing plate, 16- drainage conduit.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other Embodiment shall fall within the protection scope of the present invention.
Please refer to Fig. 1~3, in the embodiment of the present invention, a kind of oxalic acid bioengineering separation equipment, including body 12, it is described Body 12 is enclosed cylindrical tube structure, and the bottom outer ring of body 12 is provided with more supporting legs 3, passes through supporting leg 3 Body 12 can be stablized and support, the inside upper part of the body 12 is equipped with deflector 6, and deflector 6 is up big and down small taper Structure cylinder, the upper end of deflector 6 are smoothly connected with the inner sidewall parabola of body 12, and the upside space of deflector 6 is preliminary Disengagement chamber 11, the upside of the deflector 6 are provided with separating plate 10, and separating plate 10 is pyramidal structure, and separating plate 10 and water conservancy diversion Plate 6 is arranged in parallel, and the vertical range between separating plate 10 and deflector 6 is 10-20cm, and the upper end diameter of separating plate 10 is body The 1/2 of 12 internal diameters, the inside of the separating plate 10 are provided with carrying web plate 7, and carrying web plate 7 is netted made of stainless steel material Structure, carrying web plate 7 are middle part arc concave configuration, and the inner wall parabola of the outer ring and separating plate 10 that carry web plate 7 smoothly connects It connects, filtering out for waste liquid is conducive to by carrying web plate 7, the centre of the separating plate 10 is equipped with central axis 5, the outer diameter of central axis 5 It is the 1/2 of 6 lower end diameter of deflector, the lower end of central axis 5 is stretched out from the bottom of body 12, the bottom of central axis 5 and body 12 Sealing rotation connection, the bottom of the body 12 is additionally provided with the driving motor 2 connecting with central axis 5, can be driven by driving motor 2 Dynamic central axis 5 rotates.
The downside of the deflector 6 is outer ring in being equipped with secondary separation web plate 13, secondary separation web plate 13 on central axis 5 Tilt down the pyramidal structure of setting, secondary separation web plate 13 is reticular structure made of stainless steel material, and secondary separation net The mesh of plate 13 is identical with the carrying mesh size shape of web plate 7, can separate oxalic acid particle and waste liquid, the secondary separation The diameter of web plate 13 is less than the internal diameter of body 12, and the downside of secondary separation web plate 13 is in being mounted with storage on 12 inner sidewall of body Flitch 15, the storing plate 15 include the cylindrical tube on top and the conical shell of lower part, and the outer diameter of cylindrical tube is less than The diameter of secondary separation web plate 13, the lower end of conical shell and the inner sidewall of body 12 are connected and fixed, the storing plate 15 and machine Body 12 constitute space be storage cavity 14, for the storage of oxalic acid particle, be circumferentially on the side wall of the body 12 it is multiple with The drainage conduit 16 of 14 bottom of storage cavity connection, the discharge of oxalic acid particle is used for by drainage conduit 16.
Several discard solution discharge ports 4 are offered on the central axis 5, discard solution discharge port 4 passes through the channel opened up in central axis 5 (not shown) is connected to the space in separating plate 10, and the waste water in separating plate 10 can flow into the channel of central axis 5, after from waste liquid Discharge outlet 4 is discharged, and the discard solution discharge port 4 is located at the downside of 15 upper surface of storing plate, the water body for avoiding discard solution discharge port 4 from being discharged It is splashed into storage cavity 14, the top center of the body 12 is also equipped with feed pipe 8, the lower end of feed pipe 8 and carrying web plate 7 Vertical range be 10-20cm, the upper end of feed pipe 8 is equipped with hopper 9, facilitates the addition of material, the body by hopper 9 12 bottom is additionally provided with the sewer pipe 1 being discharged for waste liquid in body 12.
Raw material oxalic acid is dissolved in the sulfate liquor of 37 ° of B é in a kettle, after completely dissolution, obtains oxalic acid mother liquor, reacted Temperature in kettle is 57 DEG C, by oxalic acid mother liquor in equipment of crystallisation by cooling continuous crystallisation it is cold so that oxalic acid crystallization is oxalic acid particle But the temperature in crystallization apparatus is 25 DEG C, and the substance in equipment of crystallisation by cooling is centrifuged (in grass described herein Carried out in sour bioengineering separation equipment), oxalic acid particle and waste liquid are obtained, oxalic acid particle is dried under the conditions of 68 DEG C, obtains purity For 99.5% oxalic acid.
The oxalic acid bioengineering separation equipment, the substance in equipment of crystallisation by cooling is added in hopper 9, after pass through charging Pipe 8 drops on carrying web plate 7, and waste liquid can be filtered out by carrying web plate 7, and be flowed by the discard solution discharge port 4 on central axis 5 Out, it drives central axis 5 to rotate by driving motor 2, and then separating plate 10 rotates, may make the substance centrifugation on carrying web plate 7 Separation, the oxalic acid particle isolated can fall on deflector 6, by the structure setting of deflector 6, be slipped to conducive to oxalic acid particle On secondary separation web plate 13, by secondary separation web plate 13 can secondary separation go out the waste liquid in oxalic acid particle, rear oxalic acid particle can It drops into storage cavity 14 and collects, waste liquid that discard solution discharge port 4 is discharged and from 13 2 waste liquids filtered out of secondary separation web plate It can be collected by the bottom space of body 12;Whole device is compact-sized, and space occupied is small, the oxalic acid gone out by secondary separation Grain is less containing waste liquid, and regular shape, and processing quality is good, high-efficient, promotes the performance of enterprises, is conducive to investment application.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims Variation is included within the present invention.Any reference signs in the claims should not be construed as limiting the involved claims.
The above are merely the preferred embodiment of the present invention, it is noted that for those skilled in the art, not Under the premise of being detached from present inventive concept, several modifications and improvements can also be made, these also should be considered as protection model of the invention It encloses, these all will not influence the effect and patent practicability that the present invention is implemented.

Claims (10)

1. a kind of oxalic acid bioengineering separation equipment, including body (12), body (12) is enclosed cylindrical tube structure, The bottom outer ring of body (12) is provided with more supporting legs (3), which is characterized in that the inside upper part of the body (12) is equipped with Deflector (6), the upside space of deflector (6) are initial gross separation chamber (11), are provided with separating plate on the upside of the deflector (6) (10), carrying web plate (7) is provided on the inside of the separating plate (10), the centre of the separating plate (10) is equipped with central axis (5), the bottom of body (12) is additionally provided with the driving motor (2) connecting with central axis (5);
The downside of the deflector (6) in being equipped with secondary separation web plate (13) on central axis (5), secondary separation web plate (13) Downside is mounted with storing plate (15) on body (12) inner sidewall, the space of the storing plate (15) and body (12) composition For storage cavity (14);
It is offered several discard solution discharge ports (4) on the central axis (5), discard solution discharge port (4) is by opening up in central axis (5) Channel is connected to the space in separating plate (10).
2. oxalic acid bioengineering separation equipment according to claim 1, which is characterized in that the deflector (6) is upper big Under small pyramidal structure cylinder, the upper end of deflector (6) and the inner sidewall parabola of body (12) are smoothly connected.
3. oxalic acid bioengineering separation equipment according to claim 1 or 2, which is characterized in that the separating plate (10) is Pyramidal structure, and separating plate (10) is arranged in parallel with deflector (6), the vertical range between separating plate (10) and deflector (6) For 10-20cm, the upper end diameter of separating plate (10) is the 1/2 of body (12) internal diameter.
4. oxalic acid bioengineering separation equipment according to claim 3, which is characterized in that the carrying web plate (7) is not Become rusty Steel material made of reticular structure, carrying web plate (7) be middle part arc concave configuration, carry web plate (7) outer ring with separate The inner wall parabola of plate (10) is smoothly connected.
5. oxalic acid bioengineering separation equipment according to claim 4, which is characterized in that the outer diameter of the central axis (5) It is the 1/2 of deflector (6) lower end diameter.
6. oxalic acid bioengineering separation equipment according to claim 5, which is characterized in that the secondary separation web plate (13) Tilt down the pyramidal structure of setting for outer ring, secondary separation web plate (13) is reticular structure made of stainless steel material, and two The mesh of secondary separation web plate (13) is identical with the carrying mesh size shape of web plate (7).
7. oxalic acid bioengineering separation equipment according to claim 6, which is characterized in that the secondary separation web plate (13) Diameter be less than body (12) internal diameter.
8. oxalic acid bioengineering separation equipment according to claim 1, which is characterized in that the storing plate (15) includes upper The cylindrical tube in portion and the conical shell of lower part, the outer diameter of cylindrical tube are less than the diameter of secondary separation web plate (13), cone The lower end of shape cylinder and the inner sidewall of body (12) are connected and fixed.
9. oxalic acid bioengineering separation equipment according to claim 1 or 8, which is characterized in that the discard solution discharge port (4) Positioned at the downside of storing plate (15) upper surface.
10. oxalic acid bioengineering separation equipment according to claim 1, which is characterized in that the top of the body (12) Centre is also equipped with feed pipe (8), and the lower end of feed pipe (8) and the vertical range of carrying web plate (7) are 10-20cm, feed pipe (8) upper end is equipped with hopper (9), and the bottom of the body (12) is additionally provided with the sewer pipe for the interior waste liquid discharge of body (12) (1), multiple drainage conduits (16) being connected to storage cavity (14) bottom are circumferentially on the side wall of the body (12).
CN201811060769.7A 2018-09-12 2018-09-12 Oxalic acid bioengineering splitter Expired - Fee Related CN109304058B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811060769.7A CN109304058B (en) 2018-09-12 2018-09-12 Oxalic acid bioengineering splitter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811060769.7A CN109304058B (en) 2018-09-12 2018-09-12 Oxalic acid bioengineering splitter

Publications (2)

Publication Number Publication Date
CN109304058A true CN109304058A (en) 2019-02-05
CN109304058B CN109304058B (en) 2021-06-18

Family

ID=65224985

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811060769.7A Expired - Fee Related CN109304058B (en) 2018-09-12 2018-09-12 Oxalic acid bioengineering splitter

Country Status (1)

Country Link
CN (1) CN109304058B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07213952A (en) * 1993-09-11 1995-08-15 Fresenius Ag Latch device for bearing assembly
JP2883883B2 (en) * 1994-06-17 1999-04-19 谷井工業株式会社 Activated dewatering cake granulator for cement wastewater
JP2004004652A (en) * 2002-03-26 2004-01-08 Konica Minolta Holdings Inc Toner manufacturing apparatus and method, toner, and production line for the toner
CN101189414A (en) * 2005-05-09 2008-05-28 阿法拉伐特木堡公司 Apparatus for the purification of gas while bleeding a crank housing
CN205020249U (en) * 2015-09-19 2016-02-10 江西江锂新材料科技有限公司 Potassium hydroxide is centrifugal separator for production and processing
CN104478693B (en) * 2014-12-23 2016-05-25 山东丰元化学股份有限公司 A kind of preparation method of refining oxalic acid
CN106475236A (en) * 2016-11-29 2017-03-08 成都聚智工业设计有限公司 A kind of sewage disposal centrifuge
CN206415233U (en) * 2017-01-22 2017-08-18 樊小琳 A kind of vertical de- liquid centrifuge
EP2352532B1 (en) * 2008-09-12 2017-10-18 Walter Pobitschka Method and device for separating blood using a centrifuge
CN107413536A (en) * 2012-02-15 2017-12-01 肯西纳什公司 Centrifuge
CN207188012U (en) * 2017-08-30 2018-04-06 天津市科盟化工工贸有限公司 A kind of separator for being used for sodium thiosulfate and waste residue

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07213952A (en) * 1993-09-11 1995-08-15 Fresenius Ag Latch device for bearing assembly
JP2883883B2 (en) * 1994-06-17 1999-04-19 谷井工業株式会社 Activated dewatering cake granulator for cement wastewater
JP2004004652A (en) * 2002-03-26 2004-01-08 Konica Minolta Holdings Inc Toner manufacturing apparatus and method, toner, and production line for the toner
CN101189414A (en) * 2005-05-09 2008-05-28 阿法拉伐特木堡公司 Apparatus for the purification of gas while bleeding a crank housing
EP2352532B1 (en) * 2008-09-12 2017-10-18 Walter Pobitschka Method and device for separating blood using a centrifuge
CN107413536A (en) * 2012-02-15 2017-12-01 肯西纳什公司 Centrifuge
CN104478693B (en) * 2014-12-23 2016-05-25 山东丰元化学股份有限公司 A kind of preparation method of refining oxalic acid
CN205020249U (en) * 2015-09-19 2016-02-10 江西江锂新材料科技有限公司 Potassium hydroxide is centrifugal separator for production and processing
CN106475236A (en) * 2016-11-29 2017-03-08 成都聚智工业设计有限公司 A kind of sewage disposal centrifuge
CN206415233U (en) * 2017-01-22 2017-08-18 樊小琳 A kind of vertical de- liquid centrifuge
CN207188012U (en) * 2017-08-30 2018-04-06 天津市科盟化工工贸有限公司 A kind of separator for being used for sodium thiosulfate and waste residue

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李东辉: "《煤矿多种经营指南》", 28 February 1991, 经济管理出版社 *

Also Published As

Publication number Publication date
CN109304058B (en) 2021-06-18

Similar Documents

Publication Publication Date Title
CN101385962A (en) Reaction filter drying apparatus with compression membrane
CN109304058A (en) A kind of oxalic acid bioengineering separation equipment
CN208115203U (en) A kind of equipment of inorganic salts freezing and crystallizing purification
CN207713681U (en) Slurry oil electrostatic separator and slurry oil electrostatic separation system
CN211133150U (en) Resin filtering device with diatomite mixing and filter assisting functions
CN212895653U (en) Production system for mica slurry chemical preparation method
CN201124063Y (en) Cyclone filter solid-liquid separator
CN210583697U (en) A vacuum concentration jar for producing chinese and western patent medicine
CN201658887U (en) Millipore filter recycling device for solid particles
CN212974400U (en) Centrifugal device of high-purity cobalt sulfate crystal for new energy battery
CN106986357A (en) A kind of pyrosulfurous acid mother liquid of sodium reclaiming system
CN108421297A (en) A kind of scraper type automatic fitration slag extractor
CN202876957U (en) Horizontal centrifuge for separating dregs and seriflux in silk noodle production process
CN210138509U (en) Solid-liquid quick separation device
CN208641982U (en) A kind of centrifugal chemical raw material solid-liquid separation system
CN216418395U (en) Coalescence dehydration oil filtering device for oil purification treatment
CN206724578U (en) A kind of cumyl peroxide drying device
CN213644529U (en) Filter equipment for raw materials production
CN209378986U (en) A kind of reaction kettle with removal of impurities separation liquid distributing device
CN211585270U (en) High-efficiency, high-yield and high-quality lightness-removing tower for producing benzoic acid
CN218491715U (en) Juice hydraulic squeezing fermentation tank
CN213555661U (en) A separation filler for rivaroxaban midbody
CN208678511U (en) It is conveniently replaceable the ink filter equipment of filter core
CN215609451U (en) Separation system for continuously producing tromethamine
CN212998805U (en) Purification device of continuous purification of high concentration plant magma

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
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20210618