JPH0356763B2 - - Google Patents
Info
- Publication number
- JPH0356763B2 JPH0356763B2 JP62222261A JP22226187A JPH0356763B2 JP H0356763 B2 JPH0356763 B2 JP H0356763B2 JP 62222261 A JP62222261 A JP 62222261A JP 22226187 A JP22226187 A JP 22226187A JP H0356763 B2 JPH0356763 B2 JP H0356763B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- slurry
- cloths
- filter cloth
- cloth
- 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.)
- Expired
Links
- 239000002002 slurry Substances 0.000 claims description 34
- 239000004744 fabric Substances 0.000 claims description 32
- 238000001914 filtration Methods 0.000 claims description 23
- 238000002347 injection Methods 0.000 claims description 20
- 239000007924 injection Substances 0.000 claims description 20
- 239000000706 filtrate Substances 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、スラリーの脱水に利用する圧搾機構
付き濾過脱水機の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an improvement of a filtration dehydrator with a squeezing mechanism used for dewatering slurry.
[従来の技術]
従来、特公昭61−47639号公報や特開昭61−
42310号公報等によつて、スラリーを脱水する圧
搾機構付き濾過脱水機が既に知られている。[Prior art] Conventionally, Japanese Patent Publication No. 47639/1983 and Japanese Patent Application Laid-open No. 1983-47639
A filtration/dehydration machine with a squeezing mechanism for dewatering slurry is already known, as disclosed in Japanese Patent No. 42310 and the like.
これらの濾過脱水機は、基本的に第3図に示す
ような構成を有するものである。すなわち、同図
に示す濾過脱水機は、前後一対の濾板1a,1b
の間に2枚の濾布2a,2bを挟んで、それらの
濾布2a,2b間に、スラリー注入管4が開口す
る濾室3設け、また一方の濾板1bの内面と濾布
2bとの間にダイヤフラム5を挟んで、周縁にお
いてそれらを互いにつき合わせ、両濾布の背後を
濾液排出管6a,6bに通過させると共に、ダイ
ヤフラム5と濾板1bの内面との間に、圧水注入
管7を連通させている。 These filtration/dehydration machines basically have a configuration as shown in FIG. That is, the filtration dehydrator shown in the figure has a pair of front and rear filter plates 1a, 1b.
Two filter cloths 2a, 2b are sandwiched between them, and a filter chamber 3 in which a slurry injection pipe 4 opens is provided between the filter cloths 2a, 2b, and the inner surface of one filter plate 1b and the filter cloth 2b are With the diaphragm 5 sandwiched between them, they are brought into contact with each other at the periphery, and the filtrate discharge pipes 6a, 6b are passed behind both filter cloths, and pressurized water is injected between the diaphragm 5 and the inner surface of the filter plate 1b. The pipe 7 is communicated.
このような圧搾機構付き濾過脱水機でスラリー
を脱水する場合、スラリー注入管4から注入した
スラリーは濾布2a,2bによつて濾過される
が、濾過が進むにつれて、ケーキ8が濾布2a,
2bの内面に堆積するので、濾室3の中央部に液
状のスラリー9が残り、そのスラリーは濾液がケ
ーキ内を通らねばならないので、ケーキ8の厚さ
が大きくなる程脱水が困難となる。 When slurry is dehydrated using such a filtration dehydrator with a squeezing mechanism, the slurry injected from the slurry injection pipe 4 is filtered by the filter cloths 2a, 2b, but as the filtration progresses, the cake 8 is separated from the filter cloths 2a, 2b.
As the slurry is deposited on the inner surface of the filter chamber 3, a liquid slurry 9 remains in the center of the filter chamber 3, and since the slurry must pass through the cake, the thicker the cake 8 becomes, the more difficult it is to dehydrate the slurry.
[発明が解決しようとする問題点]
本発明の目的は、感嘆の装置により、濾室中央
部のスラリーを早く濾過できるようにして、圧搾
機構付き濾過脱水機の濾板当りの濾過速度を高め
ることにある。[Problems to be Solved by the Invention] An object of the present invention is to enable rapid filtration of the slurry in the center of the filter chamber using an impressive device, thereby increasing the filtration speed per filter plate of a filtration dehydrator with a squeezing mechanism. There is a particular thing.
[問題点を解決するための手段]
上記目的を達成するための本発明の濾過脱水機
は、前後一対の濾板の間に、それぞれ2枚1組の
互いに重ね合せた前部濾布および後部濾布を挟む
と同時に、一方の濾板と濾布との間にダイヤフラ
ムを挟み、周縁においてそれらを互いにつき合わ
せ、各2枚の前部濾布間および後部濾布間に、そ
れぞれスラリー注入管が開口する濾室を介在させ
て、各濾飯を開放可能に前部および後部濾布を対
設固定し、前部濾布および後部濾布の背後に濾液
排出管を連通させ、ダイヤフラムと濾板の間を圧
水注入管に連通させることによつて構成される。[Means for Solving the Problems] In order to achieve the above object, the filtration dehydrator of the present invention has a front filter cloth and a rear filter cloth, each of which has a pair of front and rear filter cloths stacked on top of each other, between a pair of front and rear filter plates. At the same time, a diaphragm is sandwiched between one of the filter plates and the filter cloth, and they are butted against each other at the periphery, and slurry injection pipes are opened between each of the two front and rear filter cloths. The front and rear filter cloths are fixed opposite each other so that each filtered rice can be opened, and a filtrate discharge pipe is communicated behind the front and rear filter cloths to connect the diaphragm and the filter plate. It is configured by communicating with a pressure water injection pipe.
[作 用]
スラリーの濾過を行うに際しては、スラリーが
スラリー注入管より両濾室へ圧入され、各濾布で
濾過されて濾液排出管より排出されるが、前部濾
布と後部濾布との間に流出した濾液は、それらの
濾布間を流れて濾布周辺部に至り、再び濾布内を
通過して濾液排出管より排出される。その結果、
ケーキは前部濾布の間および後部濾布の間におい
て、各濾布の内面に堆積し、圧水注入管より圧水
を圧入することによつて、濾室内のケーキおよび
スラリーが圧搾され、スラリーが脱水される。[Function] When filtering slurry, the slurry is forced into both filter chambers from the slurry injection pipe, filtered by each filter cloth, and discharged from the filtrate discharge pipe. The filtrate flowing out during this period flows between the filter cloths, reaches the periphery of the filter cloth, passes through the filter cloth again, and is discharged from the filtrate discharge pipe. the result,
The cake is deposited on the inner surface of each filter cloth between the front filter cloth and the rear filter cloth, and the cake and slurry in the filter chamber are squeezed by injecting pressurized water from the pressure water injection pipe. The slurry is dehydrated.
従つて、濾室中央部のスラリーは速く濾過さ
れ、濾過脱水機の濾板当りの濾過速度が高められ
る。 Therefore, the slurry in the center of the filter chamber is filtered quickly, and the filtration rate per filter plate of the filter-dehydrator is increased.
[実施例]
以下に本発明の実施例について詳細に説明す
る。[Examples] Examples of the present invention will be described in detail below.
第1図及び第2図に示す濾過脱水機は、実質的
に正方形板状をなす前後一対の濾板11a,11
bを備え、それらの間に、それぞれ2枚1組の前
部濾布12a,13aおよび後部濾布12b,1
3bを挟むと同時に、濾布13bと濾板11bと
の間に、周辺に止め板15を重ねたダイヤフラム
14を挟み、周縁においてそれらを互いにつき合
わせている。そして、互いに重ね合せた前部濾布
12a,13aの間および後部濾布12b,13
bの間には、それぞれスラリー注入管17a,1
7bが開口する濾室16a,16bを介在させ
て、各濾室16a,16bを開放可能に前部濾布
12a,13aおよび後部濾布12b,13bを
対設固定し、前部濾布および後部濾布の濾板11
a,11b側に位置する濾布13a,13bの背
後、すなわち濾布13aと前部濾板11aの間お
よび濾布13bとダイヤフラム14の間に濾液排
出管18a,18bを連通させ、ダイヤフラム1
4と濾板11bの間を圧水注入管19に連通させ
ている。 The filtration dehydrator shown in FIGS. 1 and 2 has a pair of front and rear filter plates 11a, 11 substantially in the shape of a square plate.
b, and between them, a set of two front filter cloths 12a, 13a and a rear filter cloth 12b, 1 are provided.
At the same time, a diaphragm 14 with a stop plate 15 layered around the periphery is sandwiched between the filter cloth 13b and the filter plate 11b, and the diaphragm 14 is brought into contact with each other at the periphery. Between the front filter cloths 12a, 13a and the rear filter cloths 12b, 13 which are stacked on top of each other,
Between b, slurry injection pipes 17a and 1 are respectively provided.
The front filter cloths 12a, 13a and the rear filter cloths 12b, 13b are fixed opposite each other so that the filter chambers 16a, 16b can be opened, with filter chambers 16a, 16b having openings 7b interposed therebetween. Filter cloth filter plate 11
The filtrate discharge pipes 18a and 18b are communicated behind the filter cloths 13a and 13b located on the sides a and 11b, that is, between the filter cloth 13a and the front filter plate 11a and between the filter cloth 13b and the diaphragm 14, and the diaphragm 1
4 and the filter plate 11b are communicated with a pressure water injection pipe 19.
なお、濾液排出管18aは前部濾板11aに、
濾液排出管18bはダイヤフラム止め板15に、
圧水注入管19は後部濾板11bに設けている。
また、図中、20a,20bはスラリー注入管1
7a,17bに設けた注入バルブを示している。 Note that the filtrate discharge pipe 18a is connected to the front filter plate 11a,
The filtrate discharge pipe 18b is connected to the diaphragm stop plate 15,
The pressure water injection pipe 19 is provided on the rear filter plate 11b.
In addition, in the figure, 20a and 20b are slurry injection pipes 1
The injection valves provided at 7a and 17b are shown.
上記構成を有する濾過脱水機によつてスラリー
の濾過を行う場合は、濾過すべきスラリーがスラ
リー注入管17a,17bより濾室16a,16
bへ圧入(注入圧0.2〜0.8MPa)され、濾室16
a,16bはスラリーで充満する。このスラリー
は前部濾布12a,13aおよび後部濾布12
b,13bで濾過され、濾液は濾液排出管18
a,18bより排出される。また、濾液は濾布1
2aおよび濾布12bによつても濾過されるが、
その濾液は濾布12a,12bの背面、すなわち
両濾布12a,12b間を流れる。これらの濾布
12a,12bの背面は互いに接しているが、布
と布とが接触しているので、それらの間には微細
な空隙がある。濾液はその空隙を通つて、濾布周
辺部に至り、前部濾布12a,13aまたは後部
濾布12b,13bを通過して、濾液排出管18
a,18bより排出される。その結果、ケーキは
前部濾布12a,13aの間および後部濾布12
b,13bの間において、各濾布の内面に堆積す
る。 When filtering slurry with the filtration dehydrator having the above configuration, the slurry to be filtered is transferred from the slurry injection pipes 17a, 17b to the filter chambers 16a, 16.
b (injection pressure 0.2 to 0.8 MPa), filter chamber 16
a and 16b are filled with slurry. This slurry is applied to the front filter cloths 12a, 13a and the rear filter cloth 12.
b, 13b, and the filtrate is passed through the filtrate discharge pipe 18.
It is discharged from a and 18b. In addition, the filtrate is filter cloth 1
2a and filter cloth 12b,
The filtrate flows between the back surfaces of the filter cloths 12a and 12b, that is, between the two filter cloths 12a and 12b. The back surfaces of these filter cloths 12a and 12b are in contact with each other, but since the cloths are in contact with each other, there are fine gaps between them. The filtrate passes through the gap, reaches the periphery of the filter cloth, passes through the front filter cloths 12a, 13a or the rear filter cloths 12b, 13b, and enters the filtrate discharge pipe 18.
It is discharged from a and 18b. As a result, the cake is formed between the front filter cloths 12a, 13a and on the rear filter cloth 12a.
It is deposited on the inner surface of each filter cloth between b and 13b.
適当な濾過時間の後、スラリー注入バルブ20
a,20bを閉じて圧水注入管19より、圧水
(水圧1〜2MPa)を圧入する。それに伴なつて
ダイヤフラムは膨張し、濾室16a,16b内の
ケーキおよびスラリーが圧搾され、スラリーが脱
水される。濾室16a,16b内のスラリーがケ
ーキになつた時、前後部濾板11a,11bを開
き、前部濾布12a,13aおよび後部濾布12
b,13bからケーキを剥離して排出し、濾布を
洗浄することにより脱水工程は完了する。 After a suitable filtration time, the slurry injection valve 20
a and 20b are closed, and pressurized water (water pressure 1 to 2 MPa) is injected from the pressure water injection pipe 19. Along with this, the diaphragm expands, the cake and slurry in the filter chambers 16a and 16b are squeezed, and the slurry is dehydrated. When the slurry in the filter chambers 16a, 16b becomes a cake, the front and rear filter plates 11a, 11b are opened, and the front filter cloths 12a, 13a and the rear filter cloth 12 are removed.
The dewatering process is completed by peeling off the cake from b, 13b and discharging it, and washing the filter cloth.
[発明の効果]
従来の圧搾機構付き濾過脱水機では、濾過が進
むにつれて、ケーキの厚さが増し、濾過に難くな
つて、濾室中央部にスラリーが残り、脱水時間が
長くかかるという問題があるが、上述した本発明
の濾過脱水機では、前部濾布と後部濾布との間に
濾液の流通間隙があるため、濾室中央部のスラリ
ーが速く濾過され、濾板当りな濾過速度を上げる
ことができる。[Effects of the Invention] In the conventional filtration dehydrator with a squeezing mechanism, as filtration progresses, the thickness of the cake increases, making it difficult to filtrate, leaving slurry in the center of the filtration chamber, resulting in a long dehydration time. However, in the filtration dehydrator of the present invention described above, since there is a filtrate flow gap between the front filter cloth and the rear filter cloth, the slurry in the center of the filter chamber is filtered quickly, and the filtration rate per filter plate is increased. can be raised.
第1図、第2図は本発明の実施例を示し、第1
図はスラリー注入管の中心における水平断面図、
第2図は側面図であり、第3図は従来の濾過脱水
機の水平断面図である。
11a……前部濾板、11b……後部濾板、1
2a,13a……前部濾布、12b,13b……
後部濾布、14……ダイヤフラム、16a,16
b……濾室、17a,17b……スラリー注入
管、18a,18b……濾液排出管、19……圧
水注入管。
1 and 2 show embodiments of the present invention;
The figure is a horizontal cross-sectional view at the center of the slurry injection pipe.
FIG. 2 is a side view, and FIG. 3 is a horizontal sectional view of a conventional filtration/dehydrator. 11a...front filter plate, 11b...rear filter plate, 1
2a, 13a...front filter cloth, 12b, 13b...
Rear filter cloth, 14...Diaphragm, 16a, 16
b...Filter chamber, 17a, 17b...Slurry injection pipe, 18a, 18b...Filtrate discharge pipe, 19...Pressure water injection pipe.
Claims (1)
互いに重ね合せた前部濾布および後部濾布を挟む
と同時に、一方の濾板と濾布との間にダイヤフラ
ムを挟み、周縁においてそれらを互いにつき合わ
せ、各2枚の前部濾布間および後部濾布間に、そ
れぞれスラリー注入管が開口する濾室を介在させ
て、各濾室を開放可能に前部および後部濾布を対
設固定し、前部濾布および後部濾布の背後に濾液
排出管を連通させ、ダイヤフラムと濾板の間を圧
水注入管に連通させたことを特徴とする圧搾機構
付き濾過脱水機。1. A pair of front filter cloth and rear filter cloth are sandwiched between a pair of front and rear filter plates, and at the same time, a diaphragm is sandwiched between one of the filter plates and the filter cloth, and the diaphragm is sandwiched at the periphery. The front and rear filter cloths are placed opposite each other so that each filter chamber can be opened by interposing a filter chamber into which a slurry injection pipe opens between two front filter cloths and between two rear filter cloths. A filtration dehydrator with a squeezing mechanism, characterized in that a filtrate discharge pipe is connected behind the front filter cloth and the rear filter cloth, and a pressurized water injection pipe is connected between the diaphragm and the filter plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62222261A JPS6463008A (en) | 1987-09-04 | 1987-09-04 | Filtration dehydrator provided with press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62222261A JPS6463008A (en) | 1987-09-04 | 1987-09-04 | Filtration dehydrator provided with press |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6463008A JPS6463008A (en) | 1989-03-09 |
| JPH0356763B2 true JPH0356763B2 (en) | 1991-08-29 |
Family
ID=16779616
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62222261A Granted JPS6463008A (en) | 1987-09-04 | 1987-09-04 | Filtration dehydrator provided with press |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6463008A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4116874A1 (en) * | 1991-05-23 | 1992-11-26 | Hoesch & Soehne Eberhard | PLATE FILTER |
| JP6024917B2 (en) * | 2013-07-26 | 2016-11-16 | 株式会社石垣 | Filter press dewatering method |
| JP5999581B2 (en) * | 2013-03-15 | 2016-09-28 | 株式会社石垣 | Filter press |
| JP5907478B2 (en) * | 2013-03-15 | 2016-04-26 | 株式会社石垣 | Filter press filter cloth hanging device |
| JP5999580B2 (en) * | 2013-03-15 | 2016-09-28 | 株式会社石垣 | How to operate the filter press |
| JP6086325B2 (en) * | 2013-12-27 | 2017-03-01 | 株式会社石垣 | Filtrate discharge structure of filter press |
| JP6080113B2 (en) * | 2014-03-03 | 2017-02-15 | 株式会社石垣 | Filter press travel mechanism |
-
1987
- 1987-09-04 JP JP62222261A patent/JPS6463008A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6463008A (en) | 1989-03-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4222873A (en) | Plate and frame filter press having modified flow pattern method | |
| US3767052A (en) | Apparatus for supporting filter medium for filter press | |
| JPH0356763B2 (en) | ||
| JPS5584300A (en) | Pressure filter plate of filter press | |
| US20060180553A1 (en) | Method for filtering fluids and device for implementing said method | |
| US3737041A (en) | Filter press | |
| RU1820846C (en) | Process of dewatering in filter press | |
| JP3447767B2 (en) | Backwashable filter device and method for backwashing the filter | |
| WO2014142073A1 (en) | Filter press and filtering method in filter press | |
| JPH0639212A (en) | Filter and filtration method | |
| GB1344160A (en) | Filter press | |
| KR102145251B1 (en) | frame for plate and frame type filter press | |
| JP5999581B2 (en) | Filter press | |
| JPS57150410A (en) | Pressurized dehydrating method | |
| JP7634820B2 (en) | Filter press compression membrane and operation method | |
| US564422A (en) | Max dehne | |
| US1342839A (en) | Filter | |
| GB488280A (en) | Improvements in or relating to filter presses | |
| JPS63151315A (en) | Raw liquid supply method in open plate type filter | |
| JP2713336B2 (en) | Stock solution separator | |
| US1164065A (en) | Filtering process. | |
| JP2947061B2 (en) | Concentrate press | |
| GB191218195A (en) | Improvements in connection with Filter-presses to Adapt them for both Filtration and Hydraulic Pressing. | |
| JP5999580B2 (en) | How to operate the filter press | |
| GB1065840A (en) | A method of evacuating portions of unfiltered material from filter presses |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |