CN87214450U - Continuous viscose rayon-filtering machine - Google Patents

Continuous viscose rayon-filtering machine Download PDF

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Publication number
CN87214450U
CN87214450U CN 87214450 CN87214450U CN87214450U CN 87214450 U CN87214450 U CN 87214450U CN 87214450 CN87214450 CN 87214450 CN 87214450 U CN87214450 U CN 87214450U CN 87214450 U CN87214450 U CN 87214450U
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China
Prior art keywords
filter
filtering
equipment
steel wire
backwash
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Withdrawn
Application number
CN 87214450
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Chinese (zh)
Inventor
陈炳权
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Chen Bingquan
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Individual
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Priority to CN 87214450 priority Critical patent/CN87214450U/en
Publication of CN87214450U publication Critical patent/CN87214450U/en
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Abstract

The utility model discloses a continuous viscose rayon-filtering machine for filtration of man-made fiber spinning solution; a drum filter is double sided, and a plurality of drum filters of different diameters and a circular plate combine a multi-layer filtering assembly; the filtering assembly is divided into a plurality of independent filtering units by studs arranged in the drum filter; a plane turning backwashing arm for backwashing the independent filtering units orderly is arranged at the lower part of a distributing plate; multi-layer filtering surface is arranged in the limited volume of the filter chamber of the filtering machine of the utility model; the filtering ability of the viscose is as a plurality of times as the known filtering machine, two processes of filtering and pre-filtering can be simultaneously completed, and the grinding of the nozzle can be automatically compensated during the running.

Description

Continuous viscose rayon-filtering machine
The present invention is one and is used for the viscose glue continuous filter that the staple fibre spinning solution filters, it has an airtight overpressure resistant barrel, glue-feeder is arranged at the cylindrical shell bottom, gum outlet is arranged at top, in the tube revolution backwash arm that filtering surface is carried out continuous backwash is housed, revolution backwash arm links to each other with hollow drive shaft and constitutes backwash glue passage.
A kind of known continuous filter is arranged, can guarantee effective separation of viscose glue impurity.But the major part of this filter volume is occupied by the backwash arm, and filter area is limited, and need give first filtering rubber and mechanical admixture.In addition, when wearing and tearing, backwash arm suction nozzle need shut down adjustment.
Task of the present invention provides a kind of big filter amount viscose glue continuous filter, and this filter has the multiple filtration surface in limited chamber space.
Another task of the present invention is will filter and give the filtration two procedures to finish in the lump in filter.Further task of the present invention is that the wearing and tearing of backwash arm suction nozzle can compensate in running automatically.
Its solution is: filter drum is two-sided, and filter drum that several diameters are different and plectane are combined into the multiple filtration assembly, and the stud of filter drum inside is divided into the several separate filter element with filter assemblies; The plane rotation backwash arm that independent filter element is carried out the order backwash is arranged at the distribution plate bottom.
Between the plectane of filter and distribution plate,, give filter screen and form by filter screen and protecting wire net with having the rubber seal that gives filter screen; Hollow drive shaft is that lead key connects, and is equipped with and gives tight spring.
Filter of the present invention is compared with known filter, compact conformation, and the unit filter capacity can improve several times, saves the auxiliary filter plant that gives, the filtration short circuit of having avoided the suction nozzle wearing and tearing to cause.The plane suction nozzle is reliable simultaneously, and it is low to make required precision.
Accompanying drawing has been described one embodiment of the present of invention.
Accompanying drawing 1: viscose glue continuous filter front section view.
Accompanying drawing 2: filter drum front section view.
Accompanying drawing 3: K is to view in the accompanying drawing 2.
Accompanying drawing 4: B-B analyses and observe in the accompanying drawing 1.
Accompanying drawing 5: A-A analyses and observe in the accompanying drawing 1.
Accompanying drawing 6: amplify at the C place in the accompanying drawing 5.
Accompanying drawing 7: second type of viscose glue continuous filter of the present invention front section view.
Accompanying drawing 8: D-D analyses and observe in the accompanying drawing 7.
Fig. 1 shows the structure of viscose glue continuous filter.It comprises cylindrical shell 1, multiple filtration assembly 2, distribution plate 3, plane rotation backwash arm 4 and hollow drive shaft 5 etc.Cylindrical shell 1 comprises cover 6, the tube end 7, urceolus 8 and inner core 9., there is glue-feeder D at the tube end 7, and viscose glue is at pressure P 1Under enter tin at the bottom of, cover 6 has gum outlet E, filtered viscose glue is at P 2Under the pressure outside the discharge machine.
Multiple filtration assembly 2 by the different filter drum 10 to 14 of diameter with plectane 15 be combined intos.Referring to Fig. 2, filter drum is made up of two- layer bulging face 16 and 17, and the surface is covered with eyelet, and shut on top 18, and the bottom embeds in each bar cannelure of plectane 15 tops (Fig. 1).Each filter drum 10 to 14 inside is provided with stud 19 in Fig. 3, filter drum inside is divided into several independent filter chambers 20 to 27, referring to Fig. 4, these filter chambers communicate with the lonely shape passage 32 to 39 that is positioned at plectane 15 same channel bottoms, and the opening of lonely shape passage 32 to 39 is positioned at the lower surface of plectane 15.Several lonely shape passages in the same fan section of plectane 15 lower surfaces are formed the import of independent filter element viscose glue.Screw 28(Fig. 3 is arranged at stud 19 bottoms), plectane 15 and stud 19 end faces are fastening with screw 31.
Referring to Fig. 5 and Fig. 6, the filter drum outside is carried out and is covered into filter felt 29 and 30, synthetic filter felt 29,30 outer surface covers supporting steel wire net 46,47, middle U-shaped steel wire 48 location that embed, and U-shaped steel wire 48 both ends are wedge shape, vertically insert downwards the end, uniform along filter drum outer annular passage 40 to 45.At passage 44,45 places, U-shaped steel wire 48 inserts respectively between supporting steel wire net and the cylindrical shell 8,9.If adopt metal sintering filter felt can save supporting steel wire net 46,47, locate and directly insert between the metal sintering felt with the U-shaped steel wire with double side support net.
Referring to Fig. 1, Fig. 5.Between plectane 15 and plane rotation backwash arm 4, distribution plate 3 is set.Have the fan-shaped concave surface 49 of corresponding independent filter element to be liquid collecting room at distribution plate 3 upper surfaces, liquid collecting room 49 bottoms have square opening 50 and communicate with the tube end 7.Between plectane 15 and distribution plate 3, give rubber blanket 52 sealings of filter steel wire 51, in order to prevent viscose glue seepage outside neighbor set liquid chamber and machine with band.Give filter screen 51 and make the sandwich structure (not shown) with middle filter screen and two-layer protecting wire net, rubber blanket 52 is quincunx.
Referring to Fig. 1.Plane rotation backwash arm 4 is positioned at distribution plate 3 bottoms, is made of suction nozzle 53 and backwash arm 54, and plane rotation backwash arm 4 links to each other with hollow drive shaft 5, constitutes backwash glue passage, and the sliding surface of suction nozzle 53 is the plane, and this plane is vertical with hollow drive shaft 5.Plane rotation pneumatic cylinder 56 and ratchet mechanism 55 are housed on the hollow drive shaft 5, backwash arm suction nozzle 53 (is controlled by the time relay and operated pneumatic valve) by certain hour at interval along distribution plate 3 lower surfaces made the plane intermittent-rotation, block each square opening 50 successively, the square opening that is blocked carries out backwash, all the other square openings filter (Fig. 1 left side arrow illustrates the backwash flow process, and right-hand part is a filtering process).Hollow Transmission Shafts 5 and fixed support 58 movable sealings, backwash glue discharge pipe F is equipped with on fixed support 58 tops, with P 3Pressure is discharged backwash glue.
Be equipped with on the Hollow Transmission Shafts 5 and give tight spring 57, be connected (not shown) with ratchet mechanism 55 usefulness lead keys, at suction nozzle 53 bottoms and top pressure reduction (P 1-P 2) and give tight spring 57 effects down, can be vertically from moving wear-compensating.
The another kind of version of viscose filtration machine as shown in Figure 7 and Figure 8.Its difference is inner core 9 cancellations, and plane rotation pneumatic cylinder 56 and ratchet mechanism 55 are moved on to the equipment bottom, and multiple filtration assembly system is formed by stacking up and down with most filter discs 59.Be placed with dividing plate 60 between every metafiltration dish.Supporting steel wire net 46 ', 47 ' and the filter felt 29 ', 30 '.The fan-shaped concave surface of dividing plate 60 upper and lower surfaces constitutes independent filter chamber 61, and each filter chamber 61 is worked the hollow bolt 62 that gives filter and fastening effect and connects.Hollow bolt 62 has porous wall 63, and inboard arrangement of wall given filter screen 64, gives the spiral that filter screen 64 can roll with stainless steel cloth or steel wire.
Filter disc 59 has two plectanes 65 up and down, and plectane 65 is covered with at the concave surface position of corresponding dividing plate 60 between 66, two plectanes 65 of eyelet and links to each other with short tube 67.Its endoporus is slightly larger than hollow bolt 62 external diameters, and the position of not punching between two disks 65 reinforces with muscle.The upward dish 68 and the lower wall 69 of multiple filtration assembly adopt single-decks, also are provided with rinforcement bar 70 at plastic emitting face, and seal with hollow bolt 62 with zero RunddichtringO 71.
The operation principle of filter is known: keep P in operation all the time 1>P 2>P 3, (P wherein 1-P 2) be filtered driving force, (P 2-P 3) be the backwash motive force.Keep P by known method in operation 2Constant.

Claims (10)

1, is used for the viscose glue continuous filter that the staple fibre spinning solution filters and has an airtight overpressure resistant barrel, glue-feeder is arranged at the cylindrical shell bottom, gum outlet is arranged at top, in the tube revolution backwash arm that filtering surface is carried out continuous backwash is housed, the backwash arm links to each other with hollow drive shaft and constitutes backwash glue passage, feature of the present invention is: filter drum is two-sided, and the different filter drum 10 to 14 of several diameters is combined into multiple filtration assembly 2 with plectane 15.The stud 19 of filter drum 10 to 14 inside is divided into the several separate filter element with filter assemblies 2, and the plane rotation backwash arm 4 that independent filter element is carried out the order backwash is arranged in the bottom of distribution plate 3.
2, according to the equipment of claim 1, it is characterized in that giving with band between plectane 15 and the distribution plate 3 rubber blanket 52 sealings of filter steel wire 51, give filter steel wire 51 and form by middle filter screen and two-layer protecting wire net.
3, according to the equipment of claim 1, its feature is that also hollow drive shaft 5 is that lead key connects, and is equipped with and gives tight spring 57.
4, according to the equipment of claim 1 and 3, it is characterized in that suction nozzle 53 sliding surfaces of plane rotation backwash arm 4 are the plane, this plane is vertical with hollow drive shaft 5.
5,, it is characterized in that being equipped with on the hollow drive shaft 5 plane rotation pneumatic cylinder 56 and ratchet mechanism 55 according to the equipment of claim 4.
6, according to the equipment of claim 1, plectane 15 tops have the multiple tracks cannelure, and lonely shape passage 32 to 39 is arranged in the groove, and lonely shape passage 32 to 39 openings are positioned at plectane 15 lower surfaces
7, according to the equipment of claim 1, it is characterized in that the surface shoe of filtering felt 29,30 covers supporting steel wire net 46,47, middle U-shaped steel wire 48 location that embed, U-shaped steel wire 48 both ends are wedge shape.
8, according to the equipment of claim 1, it is characterized in that multiple filtration assembly system is formed by stacking up and down with most filter discs 59, be placed with dividing plate 60 between every metafiltration dish, supporting steel wire net 46,47 ' and filter felt 29 ', 30 '.The fan-shaped concave surface of dividing plate 60 upper and lower surfaces constitutes independent filter chamber 61, and each filter chamber 61 is worked the hollow bolt 62 that gives filter and fastening effect and connects.
9, equipment according to Claim 8 is characterized in that hollow bolt 62 has porous wall 63, and inboard arrangement of wall given filter screen 64, gives the spiral that filter screen 64 can roll with stainless steel cloth or stainless steel wire.
10, according to Claim 8 with 9 equipment, it is characterized in that filter disc 59 has two plectanes 65 up and down, plectane 65 is covered with eyelet 66 at the concave surface position of corresponding dividing plate 60, link to each other with short tube 67 between two plectanes 65, its endoporus is slightly larger than hollow bolt 62 external diameters, and the position of not punching between two plectanes 65 reinforces with muscle.
CN 87214450 1987-10-17 1987-10-17 Continuous viscose rayon-filtering machine Withdrawn CN87214450U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 87214450 CN87214450U (en) 1987-10-17 1987-10-17 Continuous viscose rayon-filtering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 87214450 CN87214450U (en) 1987-10-17 1987-10-17 Continuous viscose rayon-filtering machine

Publications (1)

Publication Number Publication Date
CN87214450U true CN87214450U (en) 1988-07-20

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 87214450 Withdrawn CN87214450U (en) 1987-10-17 1987-10-17 Continuous viscose rayon-filtering machine

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CN (1) CN87214450U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102519840A (en) * 2011-12-30 2012-06-27 宜宾长毅浆粕有限责任公司 Viscose filtering resistance detection method
CN107529444A (en) * 2011-11-14 2018-01-02 阿米亚德过滤系统公司 Fluid contamination prevention system
CN108315826A (en) * 2017-12-29 2018-07-24 黎明职业大学 A kind of filter regeneration system of waste and old non-woven cloth
CN115488639A (en) * 2022-09-22 2022-12-20 深圳市华盛源机电有限公司 Intelligent numerical control multi-position processing machine for radiating fins

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107529444A (en) * 2011-11-14 2018-01-02 阿米亚德过滤系统公司 Fluid contamination prevention system
CN102519840A (en) * 2011-12-30 2012-06-27 宜宾长毅浆粕有限责任公司 Viscose filtering resistance detection method
CN108315826A (en) * 2017-12-29 2018-07-24 黎明职业大学 A kind of filter regeneration system of waste and old non-woven cloth
CN108315826B (en) * 2017-12-29 2021-06-01 黎明职业大学 Filtration regeneration system of old and useless non-woven fabrics
CN115488639A (en) * 2022-09-22 2022-12-20 深圳市华盛源机电有限公司 Intelligent numerical control multi-position processing machine for radiating fins
CN115488639B (en) * 2022-09-22 2023-07-25 深圳市华盛源机电有限公司 Intelligent numerical control multi-position processing machine for radiating fins

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Free format text: CORRECT: ADDRESS; FROM: 4TH BUILDING NO.301 IRON LION DAZHANGTUO HANGU DISTRICT TIANJIN TO: HEXI DISTRICT, TIANJIN THIRD STREET-CHI CHUANG SHOU-LI13-101

CP03 Change of name, title or address

Address after: Tianjin City, Hexi District Zhuang Jieqi SUSATO 13-101 cover three

Patentee after: Chen Bingquan

Address before: Tianjin city Hangu District Tieshi Tuo 4 Building 301

Patentee before: Chen Bingquan

C15 Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993)
RN01 Renewal of patent term
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee