CN108693187B - Dynamic circulation device for continuous sampling of loose fibers and application method thereof - Google Patents

Dynamic circulation device for continuous sampling of loose fibers and application method thereof Download PDF

Info

Publication number
CN108693187B
CN108693187B CN201810643610.1A CN201810643610A CN108693187B CN 108693187 B CN108693187 B CN 108693187B CN 201810643610 A CN201810643610 A CN 201810643610A CN 108693187 B CN108693187 B CN 108693187B
Authority
CN
China
Prior art keywords
liquid
pipeline
fiber
circulating
circulating liquid
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
CN201810643610.1A
Other languages
Chinese (zh)
Other versions
CN108693187A (en
Inventor
辛斌杰
邢文宇
邓娜
陈阳
张铮烨
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.)
Shanghai University of Engineering Science
Original Assignee
Shanghai University of Engineering Science
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 Shanghai University of Engineering Science filed Critical Shanghai University of Engineering Science
Priority to CN201810643610.1A priority Critical patent/CN108693187B/en
Publication of CN108693187A publication Critical patent/CN108693187A/en
Application granted granted Critical
Publication of CN108693187B publication Critical patent/CN108693187B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N21/00Investigating or analysing materials by the use of optical means, i.e. using sub-millimetre waves, infrared, visible or ultraviolet light
    • G01N21/84Systems specially adapted for particular applications
    • G01N21/85Investigating moving fluids or granular solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/50Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
    • B01D29/56Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/02Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • B01F25/51Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • B01F25/52Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle with a rotary stirrer in the recirculation tube
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/82Combinations of dissimilar mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/181Preventing generation of dust or dirt; Sieves; Filters
    • B01F35/187Preventing generation of dust or dirt; Sieves; Filters using filters in mixers, e.g. during venting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/712Feed mechanisms for feeding fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75Discharge mechanisms
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N21/00Investigating or analysing materials by the use of optical means, i.e. using sub-millimetre waves, infrared, visible or ultraviolet light
    • G01N21/84Systems specially adapted for particular applications
    • G01N2021/8444Fibrous material
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N21/00Investigating or analysing materials by the use of optical means, i.e. using sub-millimetre waves, infrared, visible or ultraviolet light
    • G01N21/84Systems specially adapted for particular applications
    • G01N21/85Investigating moving fluids or granular solids
    • G01N2021/8557Special shaping of flow, e.g. using a by-pass line, jet flow, curtain flow

Abstract

The invention provides a dynamic circulation device capable of being used for continuously sampling scattered fibers, which comprises a fiber throwing mechanism, a circulating liquid throwing mechanism, a solid-liquid mixing mechanism, a fiber display mechanism, a reflux mechanism and a fluid supplementing mechanism, wherein the fiber throwing mechanism and the circulating liquid throwing mechanism are respectively communicated with the solid-liquid mixing mechanism, fiber fragments are thrown into the solid-liquid mixing mechanism by the fiber throwing mechanism, circulating liquid is thrown into the solid-liquid mixing mechanism by the circulating liquid throwing mechanism, the solid-liquid mixing mechanism is communicated with the reflux mechanism through the fiber display mechanism, the mixed liquid enters the reflux mechanism through the fiber display mechanism, the circulating liquid throwing mechanism and the solid-liquid mixing mechanism are respectively communicated with the reflux mechanism, the mixed liquid flows between the circulating liquid throwing mechanism and the reflux mechanism, the reflux mechanism is communicated with the circulating liquid throwing mechanism through the fluid supplementing mechanism, and the circulating liquid in the reflux mechanism is supplemented into the circulating liquid throwing mechanism by the fluid supplementing mechanism.

Description

Dynamic circulation device for continuous sampling of loose fibers and application method thereof
Technical Field
The invention relates to a fiber image acquisition technology, in particular to a dynamic circulation device for continuously sampling loose fibers and a use method thereof.
Background
The conventional artificial fiber identification method is doped with subjective factors of people, and is easy to cause identification errors. Along with the development of image recognition technology, the computer is used for automatically recognizing the fibers, so that the speed and the accuracy of fiber recognition can be improved, and the automatic recognition of the fibers by the computer becomes a trend. In the process of fiber type identification, a large number of fiber images need to be acquired, and currently, in the process of acquiring the fiber images, a glass slide is mainly used for manufacturing a fiber sample and then the fiber sample is observed under a microscope. When a large number of scattered fibers are required to be subjected to image acquisition, the slide glass sample is required to be replaced continuously, the operation is complex, and the efficiency is low. Accordingly, there is a need for a dynamic circulation device and method for continuous sampling of loose fibers that overcomes the above-described drawbacks.
Disclosure of Invention
The invention aims to provide a dynamic circulation device for continuously sampling loose fibers and a use method thereof, so as to improve image acquisition efficiency.
The invention adopts the technical proposal for solving the technical problems that:
a dynamic circulation device for loose fiber continuous sampling, includes fiber throwing mechanism, circulating fluid throwing mechanism, solid-liquid mixing mechanism, fiber and is showing mechanism, backward flow mechanism and fluid infusion mechanism, wherein:
the fiber throwing mechanism and the circulating liquid throwing mechanism are respectively communicated with the solid-liquid mixing mechanism, fiber fragments are thrown into the solid-liquid mixing mechanism by the fiber throwing mechanism, circulating liquid is thrown into the solid-liquid mixing mechanism by the circulating liquid throwing mechanism, the fiber fragments and the circulating liquid are mixed by the solid-liquid mixing mechanism to form mixed liquid, the solid-liquid mixing mechanism is communicated with the reflux mechanism through the fiber display mechanism, the mixed liquid enters the reflux mechanism through the fiber display mechanism, the microscope and the digital camera acquire images through the fiber display mechanism, the circulating liquid throwing mechanism and the solid-liquid mixing mechanism are respectively communicated with the reflux mechanism, the circulating liquid flows through between the circulating liquid throwing mechanism and the reflux mechanism, the reflux mechanism is communicated with the circulating liquid throwing mechanism through the liquid supplementing mechanism, and the circulating liquid in the reflux mechanism is supplemented into the circulating liquid throwing mechanism through the liquid supplementing mechanism.
Specifically:
the fiber feeding mechanism comprises a fiber feeding pipe, the fiber feeding pipe is led into the solid-liquid mixing mechanism, and the fiber fragments are fed into the solid-liquid mixing mechanism through the fiber feeding pipe;
the circulating liquid throwing mechanism comprises a liquid storage barrel for containing circulating liquid, a circulating liquid inlet pipe is connected between the liquid storage barrel and the solid-liquid mixing mechanism, and the circulating liquid in the liquid storage barrel is thrown into the solid-liquid mixing mechanism through the circulating liquid inlet pipe;
the solid-liquid mixing mechanism comprises a stirring tank for containing fiber fragments and circulating liquid, the height of the stirring tank is smaller than that of the liquid storage barrel, stirring pages are arranged in the stirring tank, a fiber inlet pipe is arranged at the top of the stirring tank, the bottom end of the fiber inlet pipe is communicated with the interior of the stirring tank, the fiber fragments are put into the stirring tank through the fiber inlet pipe, one end of the circulating liquid inlet pipe is connected to the bottom of the liquid storage barrel, the other end of the circulating liquid inlet pipe is connected to the middle of the stirring tank, the circulating liquid in the liquid storage barrel is put into the stirring tank through the circulating liquid inlet pipe, and the fiber fragments and the circulating liquid are stirred by the stirring pages to form mixed liquid;
the fiber display mechanism comprises a recovery pipeline, the recovery pipeline is connected between the stirring tank and the reflux mechanism, the mixed liquid in the stirring tank enters the reflux mechanism through the recovery pipeline, an observation window for image acquisition is arranged on the side wall of the recovery pipeline, and a microscope and a digital camera acquire images of the mixed liquid in the recovery pipeline through the observation window;
the reflux mechanism comprises a recovery tank, the height of the recovery tank is smaller than that of the stirring tank and the liquid storage barrel, a primary filter screen is arranged in the recovery tank, the recovery tank is divided into an upper part and a lower part by the primary filter screen, a reflux pipeline and an overflow pipeline are arranged at the upper part of the recovery tank, the top end of the reflux pipeline is connected to the top of the stirring tank, mixed liquid in the stirring tank flows to the upper part of the recovery tank through the reflux pipeline, the top end of the overflow pipeline is connected to the top of the liquid storage barrel, circulating liquid in the liquid storage barrel flows to the upper part of the recovery tank through the overflow pipeline, and the primary filter screen is used for carrying out preliminary filtration on the mixed liquid at the upper part of the recovery tank, so that the filtered circulating liquid is stored to the lower part of the recovery tank;
the liquid supplementing mechanism comprises a liquid supplementing pipeline, the liquid supplementing pipeline is positioned between the recovery tank and the liquid storage barrel, the top end of the liquid supplementing pipeline is connected to the bottom of the liquid storage barrel, the bottom end of the liquid supplementing pipeline is connected to the bottom of the recovery tank, the middle part of the liquid supplementing pipeline is provided with a lifting pump, and the lifting pump pumps circulating liquid stored in the recovery tank into the liquid storage barrel.
Further:
a stop valve is also arranged in the fluid infusion pipeline, the stop valve is positioned at the joint of the fluid infusion pipeline and the recovery tank, and the stop valve is used for controlling the on-off of the fluid infusion pipeline; the secondary filter screen is arranged in the fluid infusion pipeline and is positioned at the inlet end of the stop valve, and the circulating fluid in the fluid infusion pipeline is further filtered by the secondary filter screen.
The using method of the device comprises the following steps:
the circulating liquid is placed in the recovery tank in advance, the stop valve is opened, the lifting pump is started simultaneously, the circulating liquid is enabled to be subjected to impurity filtering through the secondary filter screen, the circulating liquid starts to rise to the liquid storage tank along the liquid supplementing pipeline, when the liquid level is too high, the circulating liquid flows back to the recovery tank along the overflow pipeline, liquid in the liquid storage tank flows to the stirring tank along the circulating liquid inlet pipe, when the liquid level is too high in the stirring tank, mixed liquid flows back to the recovery tank along the backflow pipeline, meanwhile, cut fiber fragments are sequentially put into the stirring tank through the fiber inlet pipe, after mixing, the circulating liquid carries the fiber fragments to continuously flow along the recovery pipeline, when the fiber fragments flow to the observation window, the fiber fragments are observed through the microscope and shot and stored in the computer, the fiber fragments after shooting flow back to the recovery tank along the recovery pipeline, the primary filter screen carries out primary filtration on the fiber fragments, and the circulating liquid flowing back to the lower part of the recovery tank is guaranteed to be separated from the fiber fragments.
The invention has the advantages that:
the dynamic circulating device and the method for continuously sampling loose fibers adopt a circulating liquid inlet pipe, a recovering pipeline and a liquid supplementing pipeline to communicate a liquid storage barrel, a stirring tank and a recovering tank to form a circulating pipeline, a lifting pump drives fiber fragments to circulate in the pipeline along with circulating liquid, the purpose of continuously collecting images is achieved, meanwhile, liquid exceeding the holding capacity in the liquid storage barrel and the stirring tank can flow back to the recovering tank through a backflow pipeline and an overflow pipeline respectively, the smooth circulation process is ensured, the problems of complex operation and low efficiency of traditional sample making and observation through glass slides are solved, continuous collection of a large number of fiber images is achieved, the device is simple in structure, easy to manufacture and high in cost performance.
Drawings
Fig. 1 is a schematic structural diagram of a dynamic circulation device for continuous sampling of loose fibers according to the present invention.
Detailed Description
In order that the manner in which the above-recited features, advantages, objects and advantages of the invention are obtained, a more particular description of the invention will be rendered by reference to specific embodiments thereof which are illustrated in the appended drawings.
As shown in fig. 1, the dynamic circulation device and method for continuously sampling loose fibers provided by the invention comprise a fiber throwing mechanism, a circulating liquid throwing mechanism, a solid-liquid mixing mechanism, a fiber display mechanism, a reflux mechanism and a fluid supplementing mechanism, wherein the fiber throwing mechanism and the circulating liquid throwing mechanism are respectively communicated with the solid-liquid mixing mechanism, fiber fragments are thrown into the solid-liquid mixing mechanism by the fiber throwing mechanism, circulating liquid is thrown into the solid-liquid mixing mechanism by the circulating liquid throwing mechanism, the fiber fragments and the circulating liquid are mixed by the solid-liquid mixing mechanism to form mixed liquid, the solid-liquid mixing mechanism is communicated with the reflux mechanism through the fiber display mechanism, the mixed liquid enters the reflux mechanism through the fiber display mechanism, a microscope and a digital camera acquire images through the fiber display mechanism, the circulating liquid throwing mechanism and the solid-liquid mixing mechanism are respectively communicated with the reflux mechanism, the circulating liquid flows between the circulating liquid throwing mechanism and the reflux mechanism, the mixed liquid flows between the solid-liquid mixing mechanism and the reflux mechanism, the reflux mechanism is communicated with the circulating liquid throwing mechanism through the fluid supplementing mechanism, and the circulating liquid in the reflux mechanism is filled into the circulating liquid throwing mechanism through the circulating liquid by the fluid supplementing mechanism. The fiber feeding mechanism comprises a fiber feeding pipe 1, the fiber feeding pipe is led into the solid-liquid mixing mechanism, and the fiber fragments are fed into the solid-liquid mixing mechanism through the fiber feeding pipe; the circulating liquid throwing mechanism comprises a liquid storage barrel 2 for containing circulating liquid, a circulating liquid inlet pipe 3 is connected between the liquid storage barrel and the solid-liquid mixing mechanism, and the circulating liquid in the liquid storage barrel is thrown into the solid-liquid mixing mechanism through the circulating liquid inlet pipe; the solid-liquid mixing mechanism comprises a stirring tank 4 for containing fiber fragments and circulating liquid, the height of the stirring tank is smaller than that of the liquid storage barrel, stirring pages are arranged in the stirring tank, a fiber inlet pipe is arranged at the top of the stirring tank, the bottom end of the fiber inlet pipe is communicated with the interior of the stirring tank, the fiber fragments are put into the stirring tank through the fiber inlet pipe, one end of the circulating liquid inlet pipe is connected to the bottom of the liquid storage barrel, the other end of the circulating liquid inlet pipe is connected to the middle of the stirring tank, the circulating liquid in the liquid storage barrel is put into the stirring tank through the circulating liquid inlet pipe, and the fiber fragments and the circulating liquid are stirred by the stirring pages to form mixed liquid; the fiber display mechanism comprises a recovery pipeline 5, the recovery pipeline is connected between the stirring tank and the reflux mechanism, the mixed liquid in the stirring tank enters the reflux mechanism through the recovery pipeline, an observation window 6 for image acquisition is arranged on the side wall of the recovery pipeline, and a microscope and a digital camera acquire images of the mixed liquid in the recovery pipeline through the observation window; the reflux mechanism comprises a recovery tank 7, the height of the recovery tank is smaller than that of the stirring tank and the liquid storage barrel, a primary filter screen 8 is arranged in the recovery tank, the recovery tank is divided into an upper part and a lower part by the primary filter screen, a reflux pipeline 9 and an overflow pipeline 10 are arranged at the upper part of the recovery tank, the top end of the reflux pipeline is connected to the top of the stirring tank, the mixed liquid in the stirring tank flows to the upper part of the recovery tank through the reflux pipeline, the top end of the overflow pipeline is connected to the top of the liquid storage barrel, the circulating liquid in the liquid storage barrel flows to the upper part of the recovery tank through the overflow pipeline, and the primary filter screen is used for preliminarily filtering the mixed liquid at the upper part of the recovery tank, so that the filtered circulating liquid is stored at the lower part of the recovery tank; the fluid infusion mechanism comprises a fluid infusion pipeline 11, the fluid infusion pipeline is positioned between the recovery tank and the liquid storage barrel, the top end of the fluid infusion pipeline is connected to the bottom of the liquid storage barrel, the bottom end of the fluid infusion pipeline is connected to the bottom of the recovery tank, a lifting pump 12 is arranged in the middle of the fluid infusion pipeline, and circulating liquid stored in the recovery tank is pumped into the liquid storage barrel by the lifting pump. The liquid supplementing pipeline is also provided with a stop valve 13 which is positioned at the joint of the liquid supplementing pipeline and the recovery tank, the stop valve controls the on-off of the liquid supplementing pipeline, the liquid supplementing pipeline is also provided with a secondary filter screen 14, the secondary filter screen is positioned at the inlet end of the stop valve, and the secondary filter screen further filters the circulating liquid in the liquid supplementing pipeline. When the device is used, circulating liquid is placed in a recovery tank in advance, a stop valve is opened, a lifting pump is started, the circulating liquid is given to the circulating liquid to enable the circulating liquid to pass through a secondary filter screen to filter impurities, then the circulating liquid starts to rise to a liquid storage tank along a liquid supplementing pipeline, when the liquid level is too high, the circulating liquid flows back to the recovery tank along an overflow pipeline, liquid in the liquid storage tank flows to a stirring tank along a circulating liquid inlet pipe, when the liquid level is too high in the stirring tank, mixed liquid flows back to the recovery tank along a backflow pipeline, meanwhile, cut fiber fragments are sequentially thrown into the stirring tank through the fiber inlet pipe, after mixing, the circulating liquid carries the fiber fragments to continuously flow along the recovery pipeline, when the fiber fragments flow to an observation window, the fiber fragments are observed by a microscope and are shot and stored in a computer, the fiber fragments after shooting flow back to the recovery tank along the recovery pipeline, and primary filter screen carries out primary filtration on the fiber fragments in the recovery tank, and the separation of the circulating liquid and the fiber fragments at the lower part of the recovery tank is guaranteed. The device adopts circulating fluid feed pipe, retrieve pipeline and fluid replacement pipeline to form circulation pipeline with stock solution bucket, agitator tank and recovery tank intercommunication, drive the fibre fragment and circulate in the pipeline along with circulating fluid through the elevator pump, realize the purpose of continuous acquisition image, liquid that surpasss holding capacity in stock solution bucket and the agitator tank can be respectively through backflow pipeline and overflow pipeline backward flow to the recovery tank in simultaneously, guarantee circulation process and go on smoothly, the operation that has solved tradition and made the sample through the slide glass is observed is complicated, the inefficiency problem, realized the continuous acquisition to a large amount of fibre images, the device structure is simple and easy, easy preparation, the sexual valence relative altitude.
The above embodiments are only for illustrating the technical concept and features of the present invention, and are intended to enable those skilled in the art to understand the content of the present invention and implement the same, but not limit the scope of the present invention, and all equivalent changes or modifications made according to the spirit of the present invention should be covered in the scope of the present invention.

Claims (2)

1. A dynamic circulation device for loose fibre continuous sampling, includes fibre input mechanism, circulating fluid input mechanism, solid-liquid mixing mechanism, fibre and is showing mechanism, backward flow mechanism and fluid infusion mechanism, its characterized in that:
the fiber throwing mechanism and the circulating liquid throwing mechanism are respectively communicated with the solid-liquid mixing mechanism, fiber fragments are thrown into the solid-liquid mixing mechanism by the fiber throwing mechanism, circulating liquid is thrown into the solid-liquid mixing mechanism by the circulating liquid throwing mechanism, the fiber fragments and the circulating liquid are mixed by the solid-liquid mixing mechanism to form mixed liquid, the solid-liquid mixing mechanism is communicated with the reflux mechanism through the fiber display mechanism, the mixed liquid enters the reflux mechanism through the fiber display mechanism, the microscope and the digital camera acquire images through the fiber display mechanism, the circulating liquid throwing mechanism and the solid-liquid mixing mechanism are respectively communicated with the reflux mechanism, the circulating liquid flows through between the circulating liquid throwing mechanism and the reflux mechanism, the reflux mechanism is communicated with the circulating liquid throwing mechanism through the liquid supplementing mechanism, and the circulating liquid in the reflux mechanism is supplemented into the circulating liquid throwing mechanism through the liquid supplementing mechanism;
the fiber feeding mechanism comprises a fiber feeding pipe, the fiber feeding pipe is led into the solid-liquid mixing mechanism, and the fiber fragments are fed into the solid-liquid mixing mechanism through the fiber feeding pipe;
the circulating liquid throwing mechanism comprises a liquid storage barrel for containing circulating liquid, a circulating liquid inlet pipe is connected between the liquid storage barrel and the solid-liquid mixing mechanism, and the circulating liquid in the liquid storage barrel is thrown into the solid-liquid mixing mechanism through the circulating liquid inlet pipe;
the solid-liquid mixing mechanism comprises a stirring tank for containing fiber fragments and circulating liquid, the height of the stirring tank is smaller than that of the liquid storage barrel, stirring pages are arranged in the stirring tank, a fiber inlet pipe is arranged at the top of the stirring tank, the bottom end of the fiber inlet pipe is communicated with the interior of the stirring tank, the fiber fragments are put into the stirring tank through the fiber inlet pipe, one end of the circulating liquid inlet pipe is connected to the bottom of the liquid storage barrel, the other end of the circulating liquid inlet pipe is connected to the middle of the stirring tank, the circulating liquid in the liquid storage barrel is put into the stirring tank through the circulating liquid inlet pipe, and the fiber fragments and the circulating liquid are stirred by the stirring pages to form mixed liquid;
the fiber display mechanism comprises a recovery pipeline, the recovery pipeline is connected between the stirring tank and the reflux mechanism, the mixed liquid in the stirring tank enters the reflux mechanism through the recovery pipeline, an observation window for image acquisition is arranged on the side wall of the recovery pipeline, and a microscope and a digital camera acquire images of the mixed liquid in the recovery pipeline through the observation window;
the reflux mechanism comprises a recovery tank, the height of the recovery tank is smaller than that of the stirring tank and the liquid storage barrel, a primary filter screen is arranged in the recovery tank, the recovery tank is divided into an upper part and a lower part by the primary filter screen, a reflux pipeline and an overflow pipeline are arranged at the upper part of the recovery tank, the top end of the reflux pipeline is connected to the top of the stirring tank, mixed liquid in the stirring tank flows to the upper part of the recovery tank through the reflux pipeline, the top end of the overflow pipeline is connected to the top of the liquid storage barrel, circulating liquid in the liquid storage barrel flows to the upper part of the recovery tank through the overflow pipeline, and the primary filter screen is used for carrying out preliminary filtration on the mixed liquid at the upper part of the recovery tank, so that the filtered circulating liquid is stored to the lower part of the recovery tank;
the liquid supplementing mechanism comprises a liquid supplementing pipeline, the liquid supplementing pipeline is positioned between the recovery tank and the liquid storage barrel, the top end of the liquid supplementing pipeline is connected to the bottom of the liquid storage barrel, the bottom end of the liquid supplementing pipeline is connected to the bottom of the recovery tank, a lifting pump is arranged in the middle of the liquid supplementing pipeline, and circulating liquid stored in the recovery tank is pumped into the liquid storage barrel by the lifting pump;
a stop valve is also arranged in the fluid infusion pipeline, the stop valve is positioned at the joint of the fluid infusion pipeline and the recovery tank, and the stop valve is used for controlling the on-off of the fluid infusion pipeline;
the secondary filter screen is arranged in the fluid infusion pipeline and is positioned at the inlet end of the stop valve, and the circulating fluid in the fluid infusion pipeline is further filtered by the secondary filter screen.
2. The method of using a dynamic circulation device for continuous sampling of loose fibers according to claim 1, comprising:
the circulating liquid is placed in the recovery tank in advance, the stop valve is opened, the lifting pump is started simultaneously, the circulating liquid is enabled to be subjected to impurity filtering through the secondary filter screen, the circulating liquid starts to rise to the liquid storage tank along the liquid supplementing pipeline, when the liquid level is too high, the circulating liquid flows back to the recovery tank along the overflow pipeline, liquid in the liquid storage tank flows to the stirring tank along the circulating liquid inlet pipe, when the liquid level is too high in the stirring tank, mixed liquid flows back to the recovery tank along the backflow pipeline, meanwhile, cut fiber fragments are sequentially put into the stirring tank through the fiber inlet pipe, after mixing, the circulating liquid carries the fiber fragments to continuously flow along the recovery pipeline, when the fiber fragments flow to the observation window, the fiber fragments are observed through the microscope and shot and stored in the computer, the fiber fragments after shooting flow back to the recovery tank along the recovery pipeline, the primary filter screen carries out primary filtration on the fiber fragments, and the circulating liquid flowing back to the lower part of the recovery tank is guaranteed to be separated from the fiber fragments.
CN201810643610.1A 2018-06-21 2018-06-21 Dynamic circulation device for continuous sampling of loose fibers and application method thereof Active CN108693187B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810643610.1A CN108693187B (en) 2018-06-21 2018-06-21 Dynamic circulation device for continuous sampling of loose fibers and application method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810643610.1A CN108693187B (en) 2018-06-21 2018-06-21 Dynamic circulation device for continuous sampling of loose fibers and application method thereof

Publications (2)

Publication Number Publication Date
CN108693187A CN108693187A (en) 2018-10-23
CN108693187B true CN108693187B (en) 2023-12-19

Family

ID=63849821

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810643610.1A Active CN108693187B (en) 2018-06-21 2018-06-21 Dynamic circulation device for continuous sampling of loose fibers and application method thereof

Country Status (1)

Country Link
CN (1) CN108693187B (en)

Citations (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL6804893A (en) * 1968-04-05 1969-10-07
JPH0377603A (en) * 1989-08-18 1991-04-03 Noboru Inoue Method and device for separating two liquids
EP0671203A1 (en) * 1994-03-08 1995-09-13 Agfa-Gevaert N.V. Photographic preparation device
US5518584A (en) * 1993-06-28 1996-05-21 Aikawa Iron Works Co., Ltd. Device for detecting foreign matter in pulp suspension
US5536942A (en) * 1991-09-12 1996-07-16 Procheck Ab Method and arrangement for determining fibre properties by near-infrared-spectroscopy
JPH08278186A (en) * 1995-04-07 1996-10-22 Central Japan Railway Co Liquid level detecting method and liquid level detector
JPH09288053A (en) * 1996-02-22 1997-11-04 Hitachi Ltd Particle analyzer
FR2749658A1 (en) * 1996-06-10 1997-12-12 Centre Tech Ind Papier METHOD FOR REGULATING A PAPER PULP MILLING CHAIN AND DEVICE FOR CONTINUOUSLY MEASURING THE QUANTITY OF PARTICLES CONTAINED IN A LIQUID
DE19823695A1 (en) * 1998-05-27 1999-12-02 Voith Sulzer Papiertech Patent Method and measuring device for the quantitative detection of ingredients
US6286740B1 (en) * 1997-07-18 2001-09-11 Tsuden Kabushiki Kaisha Energy-supplying, signal-transmitting and/or material-supplying method and apparatus for linearly-traveling mechanism
JP2005062116A (en) * 2003-08-20 2005-03-10 Mitsubishi Paper Mills Ltd Monitoring method and its device of foreign substance level in pulp slurry
DE102008010764A1 (en) * 2008-02-21 2009-08-27 Thumedi Gmbh & Co. Kg Dust detection device has dust receiving unit and response unit, where dust dispersion unit is provided with dispersion liquid injection between dust receiving unit and response unit
JP2010165355A (en) * 2010-01-04 2010-07-29 Taruno Kazuo World's newest public project countermeasure device for full payment of debt exceeding nine-hundred trillion yen of nation
CN102141560A (en) * 2010-12-23 2011-08-03 中国科学院广州能源研究所 Visual gas hydrate experimental device
CN102838205A (en) * 2012-08-31 2012-12-26 乐金电子研发中心(上海)有限公司 External continuous flow aerobic granular sludge membrane bioreactor
CN103101984A (en) * 2013-02-06 2013-05-15 常涛 System for quantitatively adding medicament by water delivery pipeline
CN104651219A (en) * 2015-02-05 2015-05-27 中国科学院广州能源研究所 Device and method for preparing biological gas and liquid organic fertilizer from fruit and vegetable wastes of collecting and distributing center
JP2015166057A (en) * 2014-03-04 2015-09-24 株式会社 小川環境研究所 Device and method for sampling active sludge mixture with addition of carrier
TW201609730A (en) * 2013-12-20 2016-03-16 吉李德卡利斯託嘉有限責任公司 Polymorphic forms of a hydrochloride salt of (S)-2-(1-(9H-purin-6-ylamino)propyl)-5-fluoro-3-phenylquinazolin-4(3H)-one
WO2017117688A1 (en) * 2016-01-04 2017-07-13 Uster Technologies Ag Method and monitoring unit for monitoring a fiber stream
CN107561044A (en) * 2017-04-26 2018-01-09 中山大学 Two-phase pipeline form, measuring system, view acquisition methods, three-dimensional reconstruction method and void fraction measurement
CN207484022U (en) * 2017-10-13 2018-06-12 上海工程技术大学 A kind of device for preparing mixed type micro-nano composite cellulosic membrane
CN208420722U (en) * 2018-06-21 2019-01-22 上海工程技术大学 A kind of dynamic circulation device can be used for staple in bulk continuous sampling

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69733734T2 (en) * 1996-06-10 2006-04-13 Centre Technique de l'Industrie des Papiers, Cartons et Celluloses, Grenoble Control method for a plant for deinking a fiber suspension and apparatus for continuously measuring the amount of particles in a liquid
US7079244B2 (en) * 2002-11-18 2006-07-18 International Remote Imaging Systems, Inc. Particle analyzer with specimen tube in-line mixer
EP2415529B1 (en) * 2009-03-31 2017-08-30 National Institute of Advanced Industrial Science and Technology Carbon dioxide coating method and device therefor
PL2458367T3 (en) * 2010-11-25 2015-12-31 Mettler Toledo Gmbh Device and method for recognising solid substances in a liquid phase
JP6027321B2 (en) * 2012-03-06 2016-11-16 公益財団法人神奈川科学技術アカデミー High-speed gene amplification detector
MX2016004720A (en) * 2013-11-11 2016-12-02 Halliburton Energy Services Inc Improved determination of fluid compositions.
JP6530653B2 (en) * 2014-07-25 2019-06-12 キヤノン株式会社 Liquid discharge apparatus, imprint apparatus, and article manufacturing method
JP6497096B2 (en) * 2015-02-04 2019-04-10 富士ゼロックス株式会社 Toner adjustment mechanism and image forming apparatus

Patent Citations (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL6804893A (en) * 1968-04-05 1969-10-07
JPH0377603A (en) * 1989-08-18 1991-04-03 Noboru Inoue Method and device for separating two liquids
US5536942A (en) * 1991-09-12 1996-07-16 Procheck Ab Method and arrangement for determining fibre properties by near-infrared-spectroscopy
US5518584A (en) * 1993-06-28 1996-05-21 Aikawa Iron Works Co., Ltd. Device for detecting foreign matter in pulp suspension
EP0671203A1 (en) * 1994-03-08 1995-09-13 Agfa-Gevaert N.V. Photographic preparation device
JPH08278186A (en) * 1995-04-07 1996-10-22 Central Japan Railway Co Liquid level detecting method and liquid level detector
JPH09288053A (en) * 1996-02-22 1997-11-04 Hitachi Ltd Particle analyzer
FR2749658A1 (en) * 1996-06-10 1997-12-12 Centre Tech Ind Papier METHOD FOR REGULATING A PAPER PULP MILLING CHAIN AND DEVICE FOR CONTINUOUSLY MEASURING THE QUANTITY OF PARTICLES CONTAINED IN A LIQUID
US6286740B1 (en) * 1997-07-18 2001-09-11 Tsuden Kabushiki Kaisha Energy-supplying, signal-transmitting and/or material-supplying method and apparatus for linearly-traveling mechanism
DE19823695A1 (en) * 1998-05-27 1999-12-02 Voith Sulzer Papiertech Patent Method and measuring device for the quantitative detection of ingredients
JP2005062116A (en) * 2003-08-20 2005-03-10 Mitsubishi Paper Mills Ltd Monitoring method and its device of foreign substance level in pulp slurry
DE102008010764A1 (en) * 2008-02-21 2009-08-27 Thumedi Gmbh & Co. Kg Dust detection device has dust receiving unit and response unit, where dust dispersion unit is provided with dispersion liquid injection between dust receiving unit and response unit
JP2010165355A (en) * 2010-01-04 2010-07-29 Taruno Kazuo World's newest public project countermeasure device for full payment of debt exceeding nine-hundred trillion yen of nation
CN102141560A (en) * 2010-12-23 2011-08-03 中国科学院广州能源研究所 Visual gas hydrate experimental device
CN102838205A (en) * 2012-08-31 2012-12-26 乐金电子研发中心(上海)有限公司 External continuous flow aerobic granular sludge membrane bioreactor
CN103101984A (en) * 2013-02-06 2013-05-15 常涛 System for quantitatively adding medicament by water delivery pipeline
TW201609730A (en) * 2013-12-20 2016-03-16 吉李德卡利斯託嘉有限責任公司 Polymorphic forms of a hydrochloride salt of (S)-2-(1-(9H-purin-6-ylamino)propyl)-5-fluoro-3-phenylquinazolin-4(3H)-one
JP2015166057A (en) * 2014-03-04 2015-09-24 株式会社 小川環境研究所 Device and method for sampling active sludge mixture with addition of carrier
CN104651219A (en) * 2015-02-05 2015-05-27 中国科学院广州能源研究所 Device and method for preparing biological gas and liquid organic fertilizer from fruit and vegetable wastes of collecting and distributing center
WO2017117688A1 (en) * 2016-01-04 2017-07-13 Uster Technologies Ag Method and monitoring unit for monitoring a fiber stream
CN107561044A (en) * 2017-04-26 2018-01-09 中山大学 Two-phase pipeline form, measuring system, view acquisition methods, three-dimensional reconstruction method and void fraction measurement
CN207484022U (en) * 2017-10-13 2018-06-12 上海工程技术大学 A kind of device for preparing mixed type micro-nano composite cellulosic membrane
CN208420722U (en) * 2018-06-21 2019-01-22 上海工程技术大学 A kind of dynamic circulation device can be used for staple in bulk continuous sampling

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
The Fluid Diode: Tunable Unidirectional Flow through Porous Substrates;Joseph E. Mates et,;《ACS Applied Materials & Interfaces》;第6卷;第1-7页 *
纤维素在离子液体水溶液中的溶胀与溶解行为的研究;蔡涛;张慧慧;邵惠丽;胡学超;;合成纤维(01);第32-36页 *
纤维素纤维直径及其混纺产品成分含量测试系统;贾立锋;孟会娟;饶高咏;张洪;杨向东;;东华大学学报(自然科学版)(05);第500-505页 *
聚合物熔融机理实验研究现状;李建立 等,;《工程塑料应用》;第41卷(第10期);第105-109页 *
聚苯胺/聚乙烯醇纳米纤维的制备与表征;王香琴 等;《材料导报B:研究篇》;第28卷(第2期);第65-70页 *
麻/棉混纺纱混纺比测定的制样及纤维计数研究;张保兴;吴雄英;;上海纺织科技(01);第59-61页 *

Also Published As

Publication number Publication date
CN108693187A (en) 2018-10-23

Similar Documents

Publication Publication Date Title
CN108693187B (en) Dynamic circulation device for continuous sampling of loose fibers and application method thereof
CN113996212A (en) Honey clarifying method
CN208420722U (en) A kind of dynamic circulation device can be used for staple in bulk continuous sampling
CN108663261B (en) In a kind of water body example dissolubility can agglutinating matter filtering enriching apparatus
CN219050539U (en) Shrimp shell automatic collection device
CN209081843U (en) A kind of edible oil separating and filtering device
CN108786239A (en) Medical liquor extraction apparatus
CN215559567U (en) Multi-stage processing pressure-superposed water purifying equipment
CN205287866U (en) A recovery processing device for vacuum pump waste oil
CN213171857U (en) Rainwater collecting and circulating treatment device
CN213853182U (en) A extraction device for podophyllotoxin draws
CN209735047U (en) Oral liquid alcohol precipitation device that stews
CN103682239A (en) Novel quick-proportioning mixing liquid-feeding equipment
CN209727578U (en) A kind of filter suitable for the automatic production facility of liquid basal cell
CN208177086U (en) A kind of nicotine extraction Slag treatment device
CN211462360U (en) Oil-water separation device with filtering function for oil exploitation
CN213967122U (en) Heavy mineral separation device for diamond ore
CN205252706U (en) Tea -seed oil dregs of fat sedimentation tank
CN212662929U (en) Elution liquid medicine edulcoration system in heparin sodium production
CN218454194U (en) Adipose tissue extraction element
CN216106481U (en) Automatic control device for light alkali recycling
CN204644376U (en) A kind of classified filtering preliming tank
CN208356299U (en) A kind of recycle device of waste plastics cleaning solution
CN217221949U (en) Centrifugal equipment for obtaining high-density fat gel
CN215538587U (en) Prosthetic nutrient solution of sunken prosthetic eye tail refines device

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