CN1686618A - Centrifugal machine and its dissolving discharge method - Google Patents

Centrifugal machine and its dissolving discharge method Download PDF

Info

Publication number
CN1686618A
CN1686618A CN 200510025295 CN200510025295A CN1686618A CN 1686618 A CN1686618 A CN 1686618A CN 200510025295 CN200510025295 CN 200510025295 CN 200510025295 A CN200510025295 A CN 200510025295A CN 1686618 A CN1686618 A CN 1686618A
Authority
CN
China
Prior art keywords
centrifuge
series
dissolving
filter cake
drain pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN 200510025295
Other languages
Chinese (zh)
Inventor
毛海舫
李春丽
钱惠根
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 Institute of Technology
Original Assignee
Shanghai Institute of Technology
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 Institute of Technology filed Critical Shanghai Institute of Technology
Priority to CN 200510025295 priority Critical patent/CN1686618A/en
Publication of CN1686618A publication Critical patent/CN1686618A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Centrifugal Separators (AREA)

Abstract

A centrifugal machine is composed of centrifuger unit, the raw material inlet pipe, washing liquid inlet pipe and mother liquid outlet pipe, which are connected to said centrifuger unit, the solvent inlet tuber and the filtered cake solution outlet pipe. Its dissolving-discharging method includes such steps as dissolving the filtered cake in solvent and discharging its solution.

Description

Centrifuge and dissolving discharging method thereof
Technical field
The present invention relates to solid-liquid separation technique, particularly relate to the solid-liquid separation technique of a kind of centrifuge and dissolving discharging thereof.
Background technology
In fields such as chemical industry, medicine, food, mine, metallurgy, light textile, printing and dyeing, well-known, the centrifuge solid-phase material of Separation of Solid and Liquid, filter cake are by manually drawing off or by doctor blade device it being scraped, with the solid form discharging.Be easy with centrifuge with Separation of Solid and Liquid under normal conditions, but, certain difficulty arranged when solid transfer is gone out filter under the working condition that uses inflammable and explosive or high toxicity solvent.And solid-phase material is not final products after the Solid-Liquid Separation, will increase the labour intensity of producing thus with the material that re-uses after the dissolution with solvents in subsequent processing, increases the turnover space, and contaminated environment easily can not satisfy the needs of manufacturing condition usually.
Summary of the invention
At the shortcoming that exists in the above-mentioned prior art, technical problem to be solved by this invention provides a kind of needs that can satisfy manufacturing condition, reduce floor space, improve operating environment, improve the cleanliness factor of surrounding environment, reduce the contaminated possibility of product, the labour intensity that reduces to produce improves the centrifuge of product economy benefit and dissolves discharging method.
In order to solve the problems of the technologies described above, a kind of centrifuge provided by the present invention comprises centrifuge and the feed pipe that is connected centrifuge, cleaning solution feed tube and mother liquor drain pipe; It is characterized in that, also comprise the solvent feed tube and the filter cake lysate drain pipe that connect centrifuge.
In order to solve the problems of the technologies described above, the dissolving discharging method of a kind of centrifuge provided by the present invention, its step is as follows:
A) material to be separated is in feed pipe enters the bowl of rotation at a high speed, and under the effect in the centrifuge field of force, material is realized filtering by filter cloth (filter screen), and liquid phase is discharged through drain pipe, and solid phase then is trapped in the rotary drum;
When B) treating that the internal filtering in rotating drum cake reaches the charge of operational procedure regulation, the stop charging is washed filter cake, simultaneously cleaning solution is leached, reach separation requirement after, close the filtrate (liquid valve;
C) centrifuge low-speed running adds solvent and makes the filter cake dissolving, solution is transported to pump or vacuum makes use, finishes the one action circulation.
Utilize centrifuge provided by the invention and dissolving method, existing centrifuge is carried out architecture advances, the solid material that separation can be obtained dissolves in centrifuge inside, carry out discharging with liquid form then, can under totally enclosed condition, carry out Separation of Solid and Liquid like this, under sealing condition, wash after the Separation of Solid and Liquid, dissolving and discharging.Adopt centrifuge of the present invention can guarantee that Separation of Solid and Liquid, washing filter cakes, dissolving and discharging process carry out under totally enclosed condition, and help keeping the cleaning in production place, reduce the labour intensity of production operation simultaneously.And can carry out continuously or the carrying out washing treatment of repeated multiple times material, thereby this machine is particularly suitable for washing requirement height, the material that needs repeated multiple times to wash again;
Because this centrifuge is operated under air-tight state, thereby this machine is particularly suitable for handling the filtration washing that the existing product of inflammable and explosive, poisonous or hypertoxic danger reaches gourmet food, medicine and the biological products etc. that do not allow pollution; Can make material at the thin layer filter cake or do not have under the filter cake state and handle, thereby the processing speed on the unit are is very high, equipment is little and compact, and floor space is little; Easy and simple to handle, labour intensity is low; Good operational environment, non-environmental-pollution, no material is wandered away and is wasted, to satisfy the needs of various manufacturing conditions.
Description of drawings
Fig. 1 is the structural representation of centrifuge in the prior art;
Fig. 2 is the structural representation of centrifuge of the present invention;
Fig. 3 is the side view of AUT series centrifuge in the prior art;
Fig. 4 is the side view of the AUT series centrifuge of the embodiment of the invention;
Fig. 5 is the vertical view of AUT series centrifuge in the prior art;
Fig. 6 is the vertical view of the AUT series centrifuge of the embodiment of the invention;
Fig. 7 is the side view of LGZ series centrifuge in the prior art;
Fig. 8 is the side view of the LGZ series centrifuge of the embodiment of the invention;
Fig. 9 is the vertical view of LGZ series centrifuge in the prior art;
Figure 10 is the vertical view of the LGZ series centrifuge of the embodiment of the invention;
Figure 11 is the side view of SGZ series centrifuge in the prior art;
Figure 12 is the side view of the SGZ series centrifuge of the embodiment of the invention;
Figure 13 is the vertical view of SGZ series centrifuge in the prior art;
Figure 14 is the vertical view of the SGZ series centrifuge of the embodiment of the invention.
The specific embodiment
Below in conjunction with description of drawings embodiments of the invention are described in further detail, but present embodiment is not limited to the present invention, every employing analog structure of the present invention and similar variation thereof all should be listed protection scope of the present invention in.
Centrifuge of the prior art comprises centrifuge 3 and the feed pipe 1 that is connected centrifuge, cleaning solution feed tube 2, mother liquor drain pipe 4 and discharging opening 5 as shown in Figure 1; Centrifuge of the present invention comprises centrifuge 3 and the feed pipe 1 that is connected centrifuge, cleaning solution feed tube 2, mother liquor drain pipe 4, solvent feed tube 6 and filter cake lysate drain pipe 7 as shown in Figure 2.
An intermediate enters next reaction through behind the crystallization reaction after intermediate will dissolve in a production process; During in the prior art conventional design technological process, as shown in Figure 1, crystallization reaction liquid is through centrifuge 3, and filter cake is by manually drawing off or by doctor blade device it being scraped, pack in the container, transport to dissolution kettle or reactor limit and material is poured into finished this technical process in the still.
As shown in Figure 2, use the dissolving discharging method of the centrifuge of the embodiment of the invention, its step is as follows:
A) material to be separated is in feed pipe 1 enters centrifuge 3 rotary drums of rotation at a high speed, and under the effect in centrifuge 3 field of forces, material is realized filtering by filter cloth (filter screen), and liquid phase is discharged through drain pipe 4, and solid phase then is trapped in the rotary drum;
When B) treating that the internal filtering in rotating drum cake reaches the charge of operational procedure regulation, the stop charging is washed filter cake, simultaneously cleaning solution is leached, reach separation requirement after, close the filtrate (liquid valve;
C) centrifuge 3 low-speed runnings add solvents through solvent feed tube 6 and make the filter cake dissolving, solution is transported to through filter cake lysate drain pipe 7 usefulness pumps or vacuum makes use, finish the one action circulation;
So implement technological process of the present invention, the labour intensity that transports after the solid discharging can be reduced, and the turnover space, and the cleanliness factor of surrounding environment can be improved, reduce environmental pollution.
Centrifuge of the present invention can adopt AUT series, LGZ series, SGZ series, SS series, SB series, PSB series to be changed.
AUT series, LGZ series, SGZ series centrifuge are scraper bottom discharging automatic centrifuges, as long as its scraper discharging device is not installed, and lower discharge port is airtight, top increases a solvent feed pipe or from the sluicing pipe solubilizer, main feature is to adopt PLC control, program setting, the automation mechanized operation of unmanned nurse, reinforced, prefiltration, washing, the smart filtration, the monitoring of solubilizer overall process; Frequency control starts steadily, and separation factor is adjustable; The totally-enclosed structure, seal adopts silicon rubber or fluorubber, and the nitrogen protection of centrifuge inner chamber can realize the tight anti-explosion requirement; The auto-action element adopts pneumatic system, sanitation and hygiene; Online washing system has guaranteed the cleanliness factor requirement, meets GMP standard etc.
Referring to Fig. 4, shown in Figure 6, AUT series centrifuge is provided with filter cake discharging opening 9 as shown in Figure 3 in the prior art about the embodiment of AUT series centrifuge in the present invention, and AUT series centrifuge of the present invention seals lower discharge port 10 as shown in Figure 4; AUT series centrifuge is provided with scraper 19 as shown in Figure 5 in the prior art, and AUT series centrifuge of the present invention is provided with solvent feed tube 20 as shown in Figure 6; Fig. 5, AUT series centrifuge shown in Figure 6 also are provided with inspection opening 11, liquid outlet 12, nitrogen air inlet pipe 13, feed pipe 14, material range controller 15, motor 16, sluicing pipe 17 and cleaning hose 18.
Referring to Fig. 8, shown in Figure 10, LGZ series centrifuge is provided with filter cake discharging opening 21 as shown in Figure 7 in the prior art about the embodiment of LGZ series centrifuge in the present invention, and LGZ series centrifuge of the present invention seals lower discharge port 22 as shown in Figure 8; LGZ series centrifuge is provided with scraper 32 as shown in Figure 9 in the prior art, and LGZ series centrifuge of the present invention is provided with exhaust outlet 33 and solvent feed tube 34 as shown in figure 10; Fig. 9, LGZ series centrifuge shown in Figure 10 also are provided with material range controller 23, liquid outlet 24, nitrogen air inlet pipe 25, feed pipe 26, illumination holes 27, motor 28, sluicing pipe 29, cleaning hose 30 and inspection opening 31.
Referring to Figure 12, shown in Figure 14, SGZ series centrifuge is provided with filter cake discharging opening 36 as shown in figure 11 in the prior art about the embodiment of SGZ series centrifuge in the present invention, and SGZ series centrifuge of the present invention seals lower discharge port 37 as shown in figure 12; SGZ series centrifuge is provided with scraper 47 as shown in figure 13 in the prior art, and SGZ series centrifuge of the present invention is provided with exhaust outlet 49 and solvent feed tube 48 as shown in figure 14; Fig. 9, SGZ series centrifuge shown in Figure 10 also are provided with inspection opening 38, material range controller 39, liquid outlet 40, nitrogen air inlet pipe 41, feed pipe 42, illumination holes 43, motor 44, cleaning hose 45 and sluicing pipe 46.
SS series, SB series centrifuge are the 3-foot upper unloading centrifuges, as long as top increases a solvent feed pipe or from the sluicing pipe solubilizer, main feature is to adopt frequency control, start steadily, and separation factor is adjustable; Contactless energy consumption braking system; The antistatic belt transmission; The body closed structure, seal adopts silicon rubber or fluorubber, can realize the tight anti-explosion requirement; The configuration nitrogen protecting system can guarantee the isolation of centrifuge inner chamber and extraneous air; Dispose online washing system, guaranteed the cleanliness factor requirement, meet GMP standard etc.
PSB series centrifuge is flat upper unloading centrifuge, as long as top increases a solvent feed pipe or from the sluicing pipe solubilizer, main feature is to adopt frequency control, starts steadily, and separation factor is adjustable; Contactless energy consumption braking system; The antistatic belt transmission; The body closed structure, seal adopts silicon rubber or fluorubber, can realize the tight anti-explosion requirement; Foundation-free is installed, and the Equipment Foundations balance plate can be used as operating platform again; The configuration nitrogen protecting system can guarantee the isolation of centrifuge inner chamber and extraneous air; Dispose online washing system, guaranteed the cleanliness factor requirement, meet GMP standard etc.

Claims (3)

1. a centrifuge comprises centrifuge and the feed pipe that is connected centrifuge, cleaning solution feed tube and mother liquor drain pipe; It is characterized in that, also comprise the solvent feed tube and the filter cake lysate drain pipe that connect centrifuge.
2. centrifuge according to claim 1 is characterized in that described centrifuge is provided with exhaust outlet.
3. the dissolving discharging method of a centrifuge is characterized in that, the step of method is as follows:
A) material to be separated is in feed pipe enters the bowl of rotation at a high speed, and material is realized filtering by filter cloth (filter screen), and liquid phase is discharged through drain pipe, and solid phase then is trapped in the rotary drum;
When B) treating that the internal filtering in rotating drum cake reaches the charge of operational procedure regulation, stop charging, filter cake washed, simultaneously cleaning solution is leached, reach separation requirement after, close the filtrate (liquid valve;
C) centrifuge low-speed running adds solvent and makes the filter cake dissolving, solution is transported to pump or vacuum makes use, finishes the one action circulation.
CN 200510025295 2005-04-21 2005-04-21 Centrifugal machine and its dissolving discharge method Pending CN1686618A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200510025295 CN1686618A (en) 2005-04-21 2005-04-21 Centrifugal machine and its dissolving discharge method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200510025295 CN1686618A (en) 2005-04-21 2005-04-21 Centrifugal machine and its dissolving discharge method

Publications (1)

Publication Number Publication Date
CN1686618A true CN1686618A (en) 2005-10-26

Family

ID=35304660

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200510025295 Pending CN1686618A (en) 2005-04-21 2005-04-21 Centrifugal machine and its dissolving discharge method

Country Status (1)

Country Link
CN (1) CN1686618A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107033261A (en) * 2017-05-08 2017-08-11 新疆中泰新鑫化工科技股份有限公司 Chliorinated polyvinyl chloride water washing device and its method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107033261A (en) * 2017-05-08 2017-08-11 新疆中泰新鑫化工科技股份有限公司 Chliorinated polyvinyl chloride water washing device and its method

Similar Documents

Publication Publication Date Title
KR100332032B1 (en) Vacuum Rotary Dryer
CN200945243Y (en) Multifunctional drying device
WO2012138048A2 (en) Filtering and drying apparatus for slurry and resource recycling
CN201644093U (en) Reaction and filter dryer
CN101780439B (en) Unloading device of centrifuge
CN112371069B (en) Continuous reaction, crystallization, filtration, washing and drying system
CN202951321U (en) Automatic vacuum feeding, washing discharging, vacuum filtering and washing device
CN113262739B (en) Hydraulic extrusion method integrating reaction crystallization, slurry washing, filtering and drying functions
CN208878816U (en) Increment system two stage centrifugal machine is recycled in a kind of
CN102826939B (en) Continuous aftertreatment technology for DPT (N,N-dipropyltryptamine) chemical product
RU2650188C1 (en) Solvent exchanger and method for improving of solvent exchange efficiency
CN101380611A (en) Filter dehydration --- dray integration centrifugal machine
CN201187939Y (en) Three-in-one multifunctional drying apparatus
CN101307981A (en) Three-in-one multifunctional drying apparatus
CN1686618A (en) Centrifugal machine and its dissolving discharge method
CN1709545A (en) Dynamic filtering machine and filter cake treating method
JP3347962B2 (en) Filtration and drying equipment
CN207805157U (en) It is circulating be filtered, washed, drying system
CN206215388U (en) A kind of drop-down shake device for discharging and Full-automatic discharging centrifuge of vertical filter screen
CN214913864U (en) Dry trinity multifunctional equipment of toper filtration washing
CN212833409U (en) Efficient three-in-one filter press
JP2001276603A (en) Multifunctional treating device
CN2584266Y (en) Solvent type vacuum filter drying device
CN2538403Y (en) Vertical stirring washing filter
CN2568275Y (en) Pyramis filtration cone type filtering pressure filter

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication