JPH0884989A - Hollow yarn membrane type water purifier - Google Patents

Hollow yarn membrane type water purifier

Info

Publication number
JPH0884989A
JPH0884989A JP6221314A JP22131494A JPH0884989A JP H0884989 A JPH0884989 A JP H0884989A JP 6221314 A JP6221314 A JP 6221314A JP 22131494 A JP22131494 A JP 22131494A JP H0884989 A JPH0884989 A JP H0884989A
Authority
JP
Japan
Prior art keywords
water
hollow fiber
fiber membrane
tank
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
JP6221314A
Other languages
Japanese (ja)
Inventor
Takeshi Kusakabe
毅 日下部
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP6221314A priority Critical patent/JPH0884989A/en
Publication of JPH0884989A publication Critical patent/JPH0884989A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/22Controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/024Hollow fibre modules with a single potted end
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/04Hollow fibre modules comprising multiple hollow fibre assemblies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • C02F9/20Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/04Specific process operations in the feed stream; Feed pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2317/00Membrane module arrangements within a plant or an apparatus
    • B01D2317/04Elements in parallel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/04Backflushing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/12Use of permeate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Health & Medical Sciences (AREA)
  • Clinical Laboratory Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PURPOSE: To provide a miniature hollow yarn membrane type water purifier by which purified water free from fine dust and bacteria is always supplied and backwash is enabled by utilizing purified water without necessitating a water storage tank, and reliability of purification effect is excellent. CONSTITUTION: A hollow yarn membrane type water purifier 1 is equipped with an activated carbon tank 5 and a hollow yarn membrane tank and has a constitution in which the hollow yarn membrane tanks 81 , 82 are provided in parallel in the system.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、中空糸膜を装着した中
空糸膜型浄水器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hollow fiber membrane type water purifier equipped with a hollow fiber membrane.

【0002】[0002]

【従来の技術】近年、水に対する関心が高まり、水道水
等を浄化する家庭用浄水器等が広く普及されている。こ
の家庭用浄水器は、一般に活性炭を内蔵し、この活性炭
に水道水中に含まれる残留塩素やその他の有害物質,臭
いの原因となる物質等を吸着させることにより、水の味
の向上を図っているものである。しかし、このような浄
水器等では、通水を停止し長い間放置すると活性炭に残
留塩素等が吸着され、この残留塩素等による殺菌力が低
下し、更に活性炭に吸着された有機物質が富栄養状態を
形成し、一般細菌が繁殖する。このような状態で通水を
再開すると、浄水出口(又は浄水吐水管)から多量の一
般細菌が見出される。そこで、活性炭槽に繁殖した一般
細菌を浄水出口から流出させないために中空糸膜を装着
した中空糸膜型浄水器が広く実用化されている。
2. Description of the Related Art In recent years, interest in water has increased, and household water purifiers for purifying tap water and the like have become widespread. This household water purifier generally has a built-in activated carbon, and by adsorbing residual chlorine contained in tap water, other harmful substances, substances causing odor, etc., the activated carbon improves the taste of water. There is something. However, in such a water purifier, if water is stopped and left for a long time, residual chlorine and the like are adsorbed on the activated carbon, the sterilizing power due to this residual chlorine and the like is reduced, and the organic substance adsorbed on the activated carbon is eutrophic. A condition is formed and general bacteria propagate. When water flow is restarted in such a state, a large amount of general bacteria is found from the purified water outlet (or the purified water discharge pipe). Therefore, a hollow fiber membrane-type water purifier equipped with a hollow fiber membrane has been widely put into practical use in order to prevent general bacteria that have propagated in an activated carbon tank from flowing out from the purified water outlet.

【0003】以下に従来の中空糸膜型浄水器について、
図面を参照しながら説明する。図10は従来の中空糸膜
型浄水器及びその浄化状態を示す断面図である。1Aは
従来の中空糸膜型浄水器、2は水道水等の原水を供給す
る原水管、3は原水管2に接続された供給管、4は供給
管3に配設された水栓、5は活性炭6を備えた活性炭
槽、6は原水中の残留塩素やカルキ分,その他の有害物
質及び臭いの原因となる物質等を取り除く活性炭、7は
活性炭6を保持する、すなわち活性炭6の流出を防止す
るフィルタ、8Aは中空糸膜9を備えた中空糸膜槽、9
は原水中の微細なゴミや一般細菌を取り除くための中空
糸膜、10Aは中空糸膜槽8Aに接続された浄水吐水管
である。尚、下部に活性炭槽5、上部に中空糸膜槽8A
が形成されたものを浄水カートリッジと称する。
The conventional hollow fiber membrane water purifier will be described below.
This will be described with reference to the drawings. FIG. 10 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its purification state. 1A is a conventional hollow fiber membrane water purifier, 2 is a raw water pipe for supplying raw water such as tap water, 3 is a supply pipe connected to the raw water pipe 2, 4 is a faucet arranged in the supply pipe 3, 5 Is an activated carbon tank equipped with activated carbon 6, 6 is activated carbon that removes residual chlorine, chlorine, other harmful substances and substances causing odor, etc. in the raw water, and 7 holds activated carbon 6, that is, the activated carbon 6 flows out A filter to prevent, 8A is a hollow fiber membrane tank with a hollow fiber membrane 9,
Is a hollow fiber membrane for removing fine dust and general bacteria in raw water, and 10A is a clean water discharge pipe connected to the hollow fiber membrane tank 8A. The activated carbon tank 5 is at the bottom and the hollow fiber membrane tank 8A is at the top.
The one in which the water is formed is called a water purification cartridge.

【0004】以上のように構成された従来の中空糸膜型
浄水器1Aについて、以下その浄化動作を説明する。ま
ず、水栓4が“開”とされる。次に、図10中矢視する
ように、原水が原水管2から供給管3を介して浄水カー
トリッジの活性炭槽5に給水される。次に、原水は、活
性炭槽5で残留塩素やカルキ分等が取り除かれた後、フ
ィルタ7を通過して中空糸膜槽8Aに給水される。次
に、原水は、中空糸膜槽8Aで微細なゴミや一般細菌が
取り除かれた後、図10中矢視するように、浄水吐水管
10Aを介して使用者等に供給される。
The purifying operation of the conventional hollow fiber membrane type water purifier 1A having the above-described structure will be described below. First, the faucet 4 is opened. Next, as shown by the arrow in FIG. 10, raw water is supplied from the raw water pipe 2 through the supply pipe 3 to the activated carbon tank 5 of the water purification cartridge. Next, the raw water is subjected to removal of residual chlorine, chlorine and the like in the activated carbon tank 5, then passes through the filter 7 and is supplied to the hollow fiber membrane tank 8A. Next, the raw water is supplied to the user or the like via the clean water discharge pipe 10A as shown by the arrow in FIG. 10, after fine dust and general bacteria are removed in the hollow fiber membrane tank 8A.

【0005】しかしながら、中空糸膜型浄水器1Aで
は、活性炭6で残留塩素等を吸着させる他、中空糸膜9
に水道水中に含まれる微細なゴミや一般細菌を目詰まり
(又はトラップ)させて取り除くため、水源の水質によ
っては、短期間で水量が減少することがあった。また中
空糸膜9に微細なゴミ等がトラップされると、これを交
換する必要があり、交換作業が面倒で利便性に欠けると
いう問題点を有していた。そこで、中空糸膜9の寿命を
延ばすために、中空糸膜9の吐水口から水を流し、中空
糸膜9に付着した微細なゴミ等を取り除く、いわゆる逆
洗技術を採用した中空糸膜型浄水器が開発されている。
この逆洗技術を採用する中空糸膜型浄水器としては、水
道水を直接中空糸膜槽8Aに給水させるものや、浄水カ
ートリッジを通過した浄水を一旦貯水タンクに貯留しこ
れを中空糸膜槽8Aに給水させるもの等が提案されてい
る。
However, in the hollow fiber membrane type water purifier 1A, the activated carbon 6 adsorbs residual chlorine and the like, and the hollow fiber membrane 9 is used.
In addition, since fine dust and general bacteria contained in tap water are clogged (or trapped) and removed, the amount of water may decrease in a short period depending on the quality of the water source. Further, if fine dust or the like is trapped in the hollow fiber membrane 9, it is necessary to replace it, and the replacement work is cumbersome and inconvenient. Therefore, in order to extend the life of the hollow fiber membrane 9, a hollow fiber membrane type adopting a so-called backwashing technique in which water is flowed from the water outlet of the hollow fiber membrane 9 to remove fine dust and the like adhering to the hollow fiber membrane 9 A water purifier is being developed.
As a hollow fiber membrane water purifier that employs this backwashing technology, one that directly supplies tap water to the hollow fiber membrane tank 8A, or the purified water that has passed through the water purification cartridge is temporarily stored in a water storage tank. Those that supply water to 8A have been proposed.

【0006】以下に従来の逆洗機能付きの中空糸膜型浄
水器について、図面を参照しながら説明する。図11は
従来の中空糸膜型浄水器及びその浄化状態を示す断面
図、図12は従来の中空糸膜型浄水器及びその逆洗状態
を示す断面図である。2は原水管、3は供給管、4は水
栓、5は活性炭槽、6は活性炭、7はフィルタ、8Aは
中空糸膜槽、9は中空糸膜、10Aは浄水吐水管であ
り、これらは前述した従来の中空糸膜型浄水器と同様な
ものであり、同一の符号を付して説明を省略する。1
A′は従来の中空糸膜型浄水器、11Aは供給管3と浄
水吐水管10Aとを接続する原水分岐管、12Aは原水
分岐管11Aに配設された切替弁、13Aは供給管3に
配設された供給弁、14Aは浄水吐水管10Aに配設さ
れた浄水吐水弁、15Aは浄水カートリッジの中空糸膜
槽8Aに接続された洗浄水排水管、16Aは洗浄水排水
管15Aに配設された洗浄水排水弁である。
A conventional hollow fiber membrane water purifier having a backwash function will be described below with reference to the drawings. FIG. 11 is a sectional view showing a conventional hollow fiber membrane water purifier and its purified state, and FIG. 12 is a sectional view showing a conventional hollow fiber membrane water purifier and its backwashed state. 2 is a raw water pipe, 3 is a supply pipe, 4 is a faucet, 5 is an activated carbon tank, 6 is an activated carbon, 7 is a filter, 8A is a hollow fiber membrane tank, 9 is a hollow fiber membrane, and 10A is a clean water discharge pipe. Is the same as that of the conventional hollow fiber membrane type water purifier described above, and the same reference numerals are given to omit the description. 1
A'is a conventional hollow fiber membrane water purifier, 11A is a raw water branch pipe connecting the supply pipe 3 and the purified water discharge pipe 10A, 12A is a switching valve arranged in the raw water branch pipe 11A, and 13A is a supply pipe 3. Disposed supply valve, 14A is a clean water discharge valve arranged in the clean water discharge pipe 10A, 15A is a wash water drain pipe connected to the hollow fiber membrane tank 8A of the clean water cartridge, and 16A is a wash water drain pipe 15A. It is a flush water drain valve installed.

【0007】以上のように構成された従来の中空糸膜型
浄水器1Aについて、以下その動作を説明する。まず、
中空糸膜型浄水器1Aの浄化動作について説明する。ま
ず、水栓4,供給弁13A及び浄水吐水弁14Aが
“開”とされ、また切替弁12A及び洗浄水排水弁16
Aが“閉”とされる。以下、前述した従来の中空糸膜型
浄水器1Aと同様にして、使用者等に浄水が供給され
る。次に、中空糸膜型浄水器1Aの逆洗動作について説
明する。まず、水栓4,切替弁12A及び洗浄水排水弁
16Aが“開”とされ、また供給弁13A及び浄水吐水
弁14Aが“閉”とされる。次に、図11中矢視するよ
うに、原水が原水管2から供給管3,原水分岐管11
A,浄水吐水管10Aを順次介して浄水カートリッジの
中空糸膜槽8Aに給水される。次に、原水は、中空糸膜
槽8Aの中空糸膜9にトラップされた微細なゴミや一般
細菌を取り除く。次に、この中空糸膜槽8Aの中空糸膜
9を洗浄した洗浄水は、洗浄水排水管15Aを介して排
水される。
The operation of the conventional hollow fiber membrane water purifier 1A constructed as described above will be described below. First,
The purification operation of the hollow fiber membrane water purifier 1A will be described. First, the faucet 4, the supply valve 13A and the purified water spouting valve 14A are opened, and the switching valve 12A and the flush water drain valve 16 are also provided.
A is closed. Hereinafter, in the same manner as the above-described conventional hollow fiber membrane water purifier 1A, purified water is supplied to the user or the like. Next, the backwash operation of the hollow fiber membrane water purifier 1A will be described. First, the faucet 4, the switching valve 12A and the wash water drain valve 16A are opened, and the supply valve 13A and the clean water discharge valve 14A are closed. Next, as shown by the arrow in FIG. 11, raw water is fed from the raw water pipe 2 to the supply pipe 3 and the raw water branch pipe 11
Water is supplied to the hollow fiber membrane tank 8A of the water purification cartridge through A and the water purification water discharge pipe 10A sequentially. Next, the raw water removes fine dust and general bacteria trapped in the hollow fiber membrane 9 of the hollow fiber membrane tank 8A. Next, the wash water that has washed the hollow fiber membranes 9 in the hollow fiber membrane tank 8A is drained through the wash water drain pipe 15A.

【0008】更に、以下に従来の逆洗機能付きの他の中
空糸膜型浄水器について、図面を参照しながら説明す
る。図13は従来の中空糸膜型浄水器及びその浄化状態
を示す断面図、図14は従来の中空糸膜型浄水器及びそ
の逆洗状態を示す断面図である。2は原水管、3は供給
管、4は水栓、5は活性炭槽、6は活性炭、7はフィル
タ、8Aは中空糸膜槽、9は中空糸膜、10Aは浄水吐
水管、13Aは供給弁、14Aは浄水吐水弁、15Aは
洗浄水排水管、16Aは洗浄水排水弁であり、これらは
前述した従来の中空糸膜型浄水器1Aと同様なものであ
り、同一の符号を付して説明を省略する。1A″は従来
の中空糸膜型浄水器、11Bは浄水吐水管10Aから分
岐された浄水分岐管、12Bは浄水を一時貯留するため
に浄水分岐管11Bに接続された貯水タンク、13Bは
貯水タンク12Bに貯留された浄水を押し出すためのパ
ワーピストンである。
Further, another conventional hollow fiber membrane water purifier having a backwash function will be described below with reference to the drawings. FIG. 13 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its purified state, and FIG. 14 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its backwashed state. 2 is a raw water pipe, 3 is a supply pipe, 4 is a faucet, 5 is an activated carbon tank, 6 is activated carbon, 7 is a filter, 8A is a hollow fiber membrane tank, 9 is a hollow fiber membrane, 10A is a clean water discharge pipe, and 13A is a supply pipe. A valve, 14A is a clean water discharge valve, 15A is a wash water drain pipe, and 16A is a wash water drain valve. These are the same as those of the conventional hollow fiber membrane type water purifier 1A described above, and are given the same reference numerals. And the description is omitted. 1A ″ is a conventional hollow fiber membrane water purifier, 11B is a purified water branch pipe branched from the purified water discharge pipe 10A, 12B is a water storage tank connected to the purified water branch pipe 11B for temporarily storing purified water, and 13B is a water storage tank. It is a power piston for pushing out the purified water stored in 12B.

【0009】以上のように構成された従来の中空糸膜型
浄水器1Aについて、以下その動作を説明する。まず、
中空糸膜型浄水器1Aの浄化動作について説明する。ま
ず、水栓4,供給弁13A及び浄水吐水弁14Aが
“開”とされ、また洗浄水排水弁16Aが“閉”とされ
る。以下、前述した従来の中空糸膜型浄水器1Aと同様
にして、使用者等に浄水が供給される一方、浄水カート
リッジを通過した浄水は、浄水吐水管10A,浄水分岐
管11Bを順次介して貯水タンク12Bに供給され、貯
留される。次に、中空糸膜型浄水器1Aの逆洗動作につ
いて説明する。まず、洗浄水排水弁16Aが“開”とさ
れ、また水栓4,供給弁13A及び浄水吐水弁14Aが
“閉”とされる。次に、パワーピストン13Bが“O
N”される。次に、貯水タンク12Bに貯留された浄水
は、浄水分岐管11B,浄水吐水管10Aを順次介して
浄水カートリッジの中空糸膜槽8Aに給水される。以
下、前述した従来の中空糸膜型浄水器1Aと同様にし
て、中空糸膜槽8Aの中空糸膜9にトラップされた微細
なゴミや一般細菌が取り除かれた後、洗浄水が洗浄水排
水管15Aを介して排水される。
The operation of the conventional hollow fiber membrane water purifier 1A constructed as described above will be described below. First,
The purification operation of the hollow fiber membrane water purifier 1A will be described. First, the faucet 4, the supply valve 13A and the purified water discharge valve 14A are opened, and the flush water drain valve 16A is closed. Hereinafter, in the same manner as the conventional hollow fiber membrane water purifier 1A described above, purified water is supplied to the user or the like, while the purified water that has passed through the water purification cartridge is sequentially passed through the purified water discharge pipe 10A and the purified water branch pipe 11B. It is supplied and stored in the water storage tank 12B. Next, the backwash operation of the hollow fiber membrane water purifier 1A will be described. First, the flush water drain valve 16A is opened, and the faucet 4, the supply valve 13A and the purified water discharge valve 14A are closed. Next, the power piston 13B becomes "O".
Next, the purified water stored in the water storage tank 12B is supplied to the hollow fiber membrane tank 8A of the water purification cartridge through the purified water branch pipe 11B and the purified water discharge pipe 10A in order. Similar to the hollow fiber membrane water purifier 1A, after removing fine dust and general bacteria trapped in the hollow fiber membrane 9 of the hollow fiber membrane tank 8A, the wash water is drained through the wash water drain pipe 15A. To be done.

【0010】[0010]

【発明が解決しようとする課題】しかしながら上記従来
の構成では、水道水等の原水を中空糸膜槽の吐水口に給
水して逆洗する場合、逆洗に原水を使用するため、中空
糸膜の内部に微細なゴミ等がトラップされ、通水再開時
に中空糸膜の内部にトラップされたゴミ等が浄水に含有
されてしまうという問題点を有していた。また浄水を貯
水タンクに一旦貯留しこれを用いて逆洗する場合、逆洗
に大量の洗浄用水が必要であるため、大きな貯水タンク
が必要となり、装置が大型化されてしまうという問題点
を有していた。
However, in the above conventional structure, when raw water such as tap water is supplied to the outlet of the hollow fiber membrane tank for backwashing, the raw water is used for backwashing, so that the hollow fiber membrane is used. There is a problem in that fine dust and the like is trapped inside the water, and dust and the like trapped inside the hollow fiber membrane are contained in the purified water when water flow is resumed. In addition, when the purified water is once stored in a water storage tank and backwashed using it, a large amount of water for cleaning is required for backwashing, so a large water storage tank is required, which causes a problem that the device becomes large. Was.

【0011】本発明は上記従来の問題点を解決するもの
であり、常に微細なゴミや一般細菌等のない浄水を供給
でき、また貯水タンク等の必要性なく浄水を利用して逆
洗でき、浄化効果等の信頼性に優れた小型の中空糸膜型
浄水器を提供することを目的とする。
The present invention solves the above-mentioned problems of the prior art, and can always supply purified water free of fine dust and general bacteria, and can be backwashed by using purified water without the need for a water storage tank. An object of the present invention is to provide a small-sized hollow fiber membrane type water purifier having excellent reliability such as purification effect.

【0012】[0012]

【課題を解決するための手段】この目的を達成するため
に本発明の中空糸膜型浄水器は、以下の構成を有してい
る。すなわち、請求項1に記載の中空糸膜型浄水器は、
活性炭槽と、中空糸膜槽と、を備えた中空糸膜型浄水器
であって、中空糸膜槽が、系内に並列に配設されている
構成を有している。
In order to achieve this object, the hollow fiber membrane type water purifier of the present invention has the following constitution. That is, the hollow fiber membrane type water purifier according to claim 1 is
A hollow fiber membrane type water purifier comprising an activated carbon tank and a hollow fiber membrane tank, wherein the hollow fiber membrane tanks are arranged in parallel in the system.

【0013】請求項2に記載の中空糸膜型浄水器は、請
求項1に記載の中空糸膜型浄水器が、活性炭槽と各中空
糸膜槽とを接続する給水分岐管と、給水分岐管に各々配
設される給水弁と、給水分岐管から各々分岐される洗浄
水排水管と、各洗浄水排水管に各々配設される洗浄水排
水弁と、各中空糸膜槽に各々接続される浄水吐水管と、
各浄水吐水管を統合する統合吐水管と、統合吐水管に配
設される浄水吐水弁と、を備えた構成を有している。
The hollow fiber membrane water purifier according to claim 2 is the same as the hollow fiber membrane water purifier according to claim 1, wherein the hollow fiber membrane water purifier has a water supply branch pipe connecting the activated carbon tank and each hollow fiber membrane tank, and a water supply branch. Connected to each water supply valve installed in each pipe, each wash water drain pipe branched from each water supply branch pipe, each wash water drain valve installed in each wash water drain pipe, and each hollow fiber membrane tank Clean water discharge pipe,
It has the composition provided with the integrated water discharge pipe which integrates each purified water discharge pipe, and the purified water discharge valve arranged in the integrated water discharge pipe.

【0014】請求項3に記載の中空糸膜型浄水器は、請
求項1に記載の中空糸膜型浄水器が、活性炭槽と各中空
糸膜槽とを接続する給水分岐管と、給水分岐管に各々配
設される給水弁と、給水分岐管から各々分岐される洗浄
水排水管と、各洗浄水排水管に各々配設される洗浄水排
水弁と、各中空糸膜槽に各々接続される浄水吐水管と、
各浄水吐水管に配設される浄水吐水弁と、各浄水吐水管
同士を各々接続する浄水分岐管と、各浄水分岐管に各々
配設される浄水分岐弁と、各浄水吐水管を統合する統合
吐水管と、を備えた構成を有している。
According to a third aspect of the present invention, there is provided a hollow fiber membrane water purifier according to the first aspect, wherein the hollow fiber membrane water purifier comprises a water supply branch pipe connecting an activated carbon tank and each hollow fiber membrane tank, and a water supply branch. Connected to each water supply valve installed in each pipe, each wash water drain pipe branched from each water supply branch pipe, each wash water drain valve installed in each wash water drain pipe, and each hollow fiber membrane tank Clean water discharge pipe,
Integrate the purified water discharge valve arranged in each purified water discharge pipe, the purified water branch pipe connecting each purified water discharge pipes, the purified water branch valve arranged in each purified water branch pipe, and each purified water discharge pipe And an integrated water discharge pipe.

【0015】請求項4に記載の中空糸膜型浄水器は、請
求項3に記載の中空糸膜型浄水器が、各浄水吐水管同士
を接続する他の浄水分岐管と、他の浄水分岐管に配設さ
れる他の浄水分岐弁と、を備えた構成を有している。
The hollow fiber membrane type water purifier according to claim 4 is the same as the hollow fiber membrane type water purifier according to claim 3, in which the other purified water branch pipes connecting the respective purified water discharge pipes and the other purified water branch And another purified water branch valve disposed in the pipe.

【0016】ここで、中空糸膜型浄水器は、水道水等を
各家庭等に供給する原水管と活性炭槽とを接続する原水
供給管と、原水供給管に配設される水栓と、を備えても
よい。給水分岐管は下流側で中空糸膜層の配設数に応じ
て分岐されており、給水弁は、この給水分岐管の分岐部
に各々配設されている。給水分岐管の代わりに活性炭槽
と各中空糸膜槽とを各々接続する給水管を備え、この給
水管に各々給水弁を配設してもよい。統合吐水管は、使
用者等への利便性を図って1か所から吐水できるように
したものであるが、使用者等の用途によってはこの統合
吐水管を設けず浄水吐水管を外方まで延設し、この浄水
吐水管に各々浄水吐水弁を配設してもよい。中空糸膜と
は、内部が空洞の糸状のものであり、浄水器に使用され
る中空糸膜には孔径0.2μm以下の孔部が穿設されて
いるものが好適に用いられる。給水弁,洗浄水排水弁,
浄水吐水弁及び浄水分岐弁としては、電磁弁等が挙げら
れる。
Here, the hollow fiber membrane type water purifier comprises a raw water supply pipe for connecting a raw water pipe for supplying tap water or the like to each household and an activated carbon tank, and a faucet arranged in the raw water supply pipe. May be provided. The water supply branch pipe is branched on the downstream side according to the number of hollow fiber membrane layers arranged, and the water supply valve is arranged at each branch portion of the water supply branch pipe. Instead of the water supply branch pipe, a water supply pipe that connects the activated carbon tank and each hollow fiber membrane tank may be provided, and a water supply valve may be provided in each of the water supply pipes. The integrated water discharge pipe is designed so that water can be discharged from one place for the convenience of users, but depending on the use of the user, this integrated water discharge pipe is not provided and the purified water discharge pipe is extended to the outside. You may extend and you may arrange | position each purified water discharge valve in this purified water discharge pipe. The hollow fiber membrane is a hollow fiber membrane having a hollow inside, and a hollow fiber membrane used in a water purifier having a hole diameter of 0.2 μm or less is preferably used. Water supply valve, wash water drain valve,
Examples of the purified water discharge valve and the purified water branch valve include electromagnetic valves.

【0017】[0017]

【作用】この構成によって、系内に中空糸膜槽が2槽以
上並設されていることにより、少なくとも1の中空糸膜
槽で浄化された浄水を他の中空糸膜槽に供給でき、これ
により貯水タンク等を要せず中空糸膜槽の中空糸膜を浄
水で洗浄することができ、常に使用者等に浄水を供給で
きる。更に系内に中空糸膜槽が3槽以上並設されている
ことにより、使用者等に浄水を供給しながら中空糸膜槽
の洗浄を行うことができる。
With this structure, two or more hollow fiber membrane tanks are arranged side by side in the system, so that purified water purified by at least one hollow fiber membrane tank can be supplied to another hollow fiber membrane tank. As a result, the hollow fiber membrane in the hollow fiber membrane tank can be washed with purified water without the need for a water storage tank or the like, and purified water can always be supplied to users. Furthermore, by arranging three or more hollow fiber membrane tanks in parallel in the system, the hollow fiber membrane tanks can be washed while supplying purified water to the user.

【0018】[0018]

【実施例】【Example】

(実施例1)以下、本発明の第1実施例における中空糸
膜型浄水器について、図面を参照しながら説明する。図
1は本発明の第1実施例における中空糸膜型浄水器及び
その浄化状態を示す断面図、図2は本発明の第1実施例
における中空糸膜型浄水器及び一方の中空糸膜槽の逆洗
状態を示す断面図、図3は本発明の第1実施例における
中空糸膜型浄水器及び他方の中空糸膜槽の逆洗状態を示
す断面図である。2は原水管、3は供給管、4は水栓、
5は活性炭槽、6は活性炭、7はフィルタ、9は中空糸
膜であり、これらは従来例と同様なものであり、同一の
符号を付して説明を省略する。1は本発明の第1実施例
における中空糸膜型浄水器、81 ,82は中空糸膜9,
9を備えた中空糸膜槽、10は活性炭槽5と各中空糸膜
槽81 ,82 とを接続した給水分岐管、111 ,112
は給水分岐管10の分岐部に各々配設された給水弁、1
1 ,122 は給水分岐管10の分岐部から各々分岐さ
れた洗浄水排水管、131 ,132 は各洗浄水排水管1
1 ,122 に配設された洗浄水排水弁、141 ,14
2 は各中空糸膜槽81 ,82 に各々接続された浄水吐水
管、15は浄水吐水管141 ,142 を統合する、すな
わち浄水吐水管14 1 ,142 に各々分岐端が接続され
た統合吐水管、16は統合吐水管15に配設された浄水
吐水弁である。尚、給水分岐管10は下流側で分岐され
て各中空糸膜槽81 ,82 に接続されており、各給水弁
111 ,112 は給水分岐管10の分岐部に各々配設さ
れている。
 (Example 1) Hereinafter, the hollow fiber in the first example of the present invention
The membrane water purifier will be described with reference to the drawings. Figure
1 is a hollow fiber membrane type water purifier according to the first embodiment of the present invention and
FIG. 2 is a sectional view showing the purification state, and FIG. 2 is a first embodiment of the present invention.
Backwash of hollow fiber membrane water purifier and one hollow fiber membrane tank in Japan
FIG. 3 is a sectional view showing a state, and FIG. 3 shows a first embodiment of the present invention.
Shows the backwash state of the hollow fiber membrane water purifier and the other hollow fiber membrane tank.
FIG. 2 is a raw water pipe, 3 is a supply pipe, 4 is a faucet,
5 is an activated carbon tank, 6 is activated carbon, 7 is a filter, 9 is a hollow fiber
Membranes, which are similar to the conventional example and have the same
The reference numerals are given and the description is omitted. 1 is a first embodiment of the present invention
Hollow fiber membrane type water purifier in 81 , 82Is the hollow fiber membrane 9,
Hollow fiber membrane tank with 9 10 is activated carbon tank 5 and each hollow fiber membrane
Tank 81 , 82 Water supply branch pipe connected to, 111 , 112 
Is a water supply valve provided at each branch of the water supply branch pipe 10, 1
Two1 , 122 Are branched from the branch portion of the water supply branch pipe 10.
Wash water drain pipe, 131 , 132 Is each wash water drain pipe 1
Two1 , 122 Water drain valve disposed in1 , 14
2 Is each hollow fiber membrane tank 81 , 82 Purified water spout connected to each
Pipe, 15 is a clean water discharge pipe 141 , 142 To integrate
Wachi clean water discharge pipe 14 1 , 142 Each branch end is connected to
Integrated water discharge pipe, 16 is purified water disposed in the integrated water discharge pipe 15
It is a spout valve. In addition, the water supply branch pipe 10 is branched on the downstream side.
Each hollow fiber membrane tank 81 , 82 Connected to each water valve
111 , 112 Are respectively installed at the branch portions of the water supply branch pipe 10.
Have been.

【0019】以上のように構成された中空糸膜型浄水器
1について、以下その動作について図面を参照しながら
説明する。図4は中空糸膜9の浄化状態のメカニズムを
示す断面図、図5は中空糸膜の逆洗状態のメカニズムを
示す断面図である。まず、中空糸膜型浄水器1の浄化動
作を説明する。まず、水栓4,各給水弁111 ,11 2
及び浄水吐水弁16が“開”とされ、各洗浄水排水弁1
1 ,132 が“閉”とされる。次に、原水が原水管2
から供給管3を介して活性炭槽5に給水される。次に、
原水は、活性炭槽5で残留塩素やカルキ分等が取り除か
れた後、フィルタ7を通過し、その後、図1中矢視する
ように、給水分岐管10を介して各中空糸膜槽81 ,8
2 に給水される。次に、原水は、中空糸膜槽81 ,82
で微細なゴミや一般細菌が取り除かれる。すなわち、図
4中矢視するように、原水は中空糸膜槽81 ,82 の中
空糸膜9,9の注水口側から給水され吐水口に向かって
送出される際に、図4中黒丸で示す原水中に含まれる微
細なゴミや一般細菌が中空糸膜9,9の孔部にトラップ
され、取り除かれる。次に、中空糸膜槽81 ,82で浄
化された浄水は、図1中矢視するように、各浄水吐水管
141 ,142 及び統合吐水管15を順次介して使用者
等に供給される。尚、本実施例では、両方の中空糸膜槽
1 ,82 で原水を浄化する場合について説明したが、
一方の中空糸膜槽81 ,82 で原水を浄化してもよい。
Hollow fiber membrane type water purifier configured as described above
Regarding No. 1, the operation will be described below with reference to the drawings.
explain. FIG. 4 shows the mechanism of the purification state of the hollow fiber membrane 9.
Fig. 5 is a sectional view showing the mechanism of backwashing of the hollow fiber membrane.
It is sectional drawing shown. First, the purification operation of the hollow fiber membrane type water purifier 1.
Explain the work. First, the faucet 4, each water supply valve 111 , 11 2 
And the clean water discharge valve 16 is opened, and each wash water drain valve 1
Three1 , 132 Is closed. Next, raw water is raw water pipe 2
Is supplied to the activated carbon tank 5 through the supply pipe 3. next,
In the raw water, is the activated carbon tank 5 removed of residual chlorine, chlorine, etc.?
After passing through the filter 7, it passes through the filter 7, and then is viewed in the direction of arrow in FIG.
As described above, each hollow fiber membrane tank 8 is connected through the water supply branch pipe 10.1 , 8
2 Will be supplied with water. Next, the raw water is the hollow fiber membrane tank 81 , 82 
Fine dust and general bacteria are removed. That is, the figure
4 Raw water is a hollow fiber membrane tank 81 , 82 in
Water is supplied from the inlet side of the empty fiber membranes 9 and 9 toward the outlet.
When it is sent out, the
Fine dust and general bacteria are trapped in the holes of the hollow fiber membranes 9, 9.
Are removed. Next, the hollow fiber membrane tank 81 , 82Clean
The purified water, as shown by the arrow in Fig. 1, is the purified water discharge pipe.
141 , 142 And the user through the integrated spout pipe 15 sequentially
Etc. In this example, both hollow fiber membrane tanks
81 , 82 I explained about the case of purifying raw water in,
One hollow fiber membrane tank 81 , 82 Raw water may be purified with.

【0020】次に、中空糸膜型浄水器1の逆洗動作につ
いて説明する。まず、中空糸膜型浄水器1の内一方の中
空糸膜槽81 を逆洗する場合について説明する。まず、
水栓4,給水弁112 及び洗浄水排水弁131 が“開”
とされ、また給水弁111 ,洗浄水排水弁132 及び浄
水吐水弁16が“閉”とされる。次に、前述の浄化動作
と同様にして、原水は、原水管2から供給管3を介して
活性炭槽5に給水された後、活性炭槽5で残留塩素やカ
ルキ分等が取り除かれる。次に、原水は、フィルタ7を
通過後、図2中矢視するように、給水分岐管10を介し
て中空糸膜槽8 2 に給水される。次に、やはり前述の浄
化動作と同様にして、原水は、中空糸膜槽82 の中空糸
膜9で微細なゴミや一般細菌が取り除かれる。次に、図
2中矢視するように、中空糸膜槽82 で浄化された浄水
は、浄水吐水管142 ,統合吐水管15及び浄水吐水管
141 を介して他方の中空糸膜槽81 に給水される。次
に、浄水は、中空糸膜槽81 の中空糸膜9にトラップさ
れた微細なゴミや一般細菌を取り除く。すなわち、図5
中矢視するように、浄水は、中空糸膜槽81 の中空糸膜
9の吐水口側から給水され注水口側に向かって送出され
る際に、図5中黒丸で示す中空糸膜9の孔部にトラップ
された微細なゴミや一般細菌を取り除く。次に、この中
空糸膜槽81 の中空糸膜9を逆洗した洗浄水は、給水分
岐管10及び洗浄水排水管121 を介して排水される。
Next, the backwashing operation of the hollow fiber membrane water purifier 1 will be described.
And explain. First, inside one of the hollow fiber membrane water purifiers 1
Empty film tank 81 The case of backwashing will be described. First,
Faucet 4, water supply valve 112 And wash water drain valve 131 Is "open"
And the water supply valve 111 , Wash water drain valve 132 And
The water discharge valve 16 is closed. Next, the cleaning operation described above
In the same manner as above, the raw water is fed from the raw water pipe 2 through the supply pipe 3.
After water is supplied to the activated carbon tank 5, residual chlorine and carbon
Ruki etc. are removed. Next, for raw water, filter 7
After passing, as shown by the arrow in FIG.
Hollow fiber membrane tank 8 2 Will be supplied with water. Next, as mentioned above,
In the same manner as the liquefying operation, the raw water is fed into the hollow fiber membrane tank 82 Hollow fiber
The membrane 9 removes fine dust and general bacteria. Next, the figure
2 As seen from the middle arrow, hollow fiber membrane tank 82 Purified water
Is the clean water discharge pipe 142 , Integrated water discharge pipe 15 and clean water discharge pipe
141 Through the other hollow fiber membrane tank 81 Will be supplied with water. Next
The purified water is a hollow fiber membrane tank 81 Trapped in the hollow fiber membrane 9 of
Removes fine dust and general bacteria. That is, FIG.
As seen in the middle arrow, the purified water is the hollow fiber membrane tank 81 Hollow fiber membrane
Water is supplied from the spout side of 9 and is discharged toward the water spout side.
Trapped in the hole of the hollow fiber membrane 9 indicated by the black circle in FIG.
Removes fine dust and general germs. Then in this
Empty film tank 81 The washing water obtained by backwashing the hollow fiber membrane 9 of
Manifold 10 and wash water drain 121 Be drained through.

【0021】次に、中空糸膜型浄水器1の内他方の中空
糸膜槽82 を逆洗する場合について説明する。まず、水
栓4,給水弁111 及び洗浄水排水弁132 が“開”と
され、また給水弁112 ,洗浄水排水弁131 及び浄水
吐水弁16が“閉”とされる。次に、前述の浄化動作及
び逆洗動作と同様にして、原水は、原水管2から供給管
3を介して活性炭槽5に給水された後、活性炭槽5で残
留塩素やカルキ分等が取り除かれる。次に、原水は、フ
ィルタ7を通過後、図3中矢視するように、給水分岐管
10を介して中空糸膜槽81 に給水される。次に、やは
り前述の浄化動作及び逆洗動作と同様にして、原水は、
中空糸膜槽81 の中空糸膜9で微細なゴミや一般細菌が
取り除かれる。次に、図3中矢視するように、中空糸膜
槽81 で浄化された浄水は、浄水吐水管141 ,統合吐
水管15及び浄水吐水管142 を介して他方の中空糸膜
槽82 に給水される。次に、前述の逆洗動作と同様にし
て、浄水は、中空糸膜槽82 の中空糸膜9にトラップさ
れた微細なゴミや一般細菌を取り除いた後、この中空糸
膜槽82 の中空糸膜9を逆洗した洗浄水は、給水分岐管
10及び洗浄水排水管122 を介して排水される。
Next, a case where the other hollow fiber membrane tank 8 2 of the hollow fiber membrane water purifier 1 is backwashed will be described. First, the faucet 4, the water supply valve 11 1 and the wash water drain valve 13 2 are opened, and the water supply valve 11 2 , the wash water drain valve 13 1 and the clean water discharge valve 16 are closed. Next, similarly to the above-described purification operation and backwash operation, the raw water is supplied from the raw water pipe 2 through the supply pipe 3 to the activated carbon tank 5, and then the activated carbon tank 5 is subjected to removal of residual chlorine, chlorine and the like. Be done. Next, the raw water, after passing through the filter 7, is supplied to the hollow fiber membrane tank 8 1 via the water supply branch pipe 10 as shown by the arrow in FIG. Next, in the same way as the above-mentioned purification operation and backwash operation, the raw water is
The hollow fiber membrane 9 in the hollow fiber membrane tank 8 1 removes fine dust and general bacteria. Next, as shown by the arrow in FIG. 3, the purified water purified in the hollow fiber membrane tank 8 1 passes through the purified water discharge pipe 14 1 , the integrated discharge pipe 15 and the purified water discharge pipe 14 2 to the other hollow fiber membrane tank 8 1. Water is supplied to 2 . Next, in the same manner as the backwash operation described above, purified water, after removing the trapped fine dust and general bacteria in the hollow fiber membrane 9 of the hollow fiber membrane tank 82, of the hollow fiber membrane tank 8 2 The wash water from which the hollow fiber membrane 9 has been backwashed is drained through the water supply branch pipe 10 and the wash water drain pipe 12 2 .

【0022】以上のように本実施例によれば、系内に中
空糸膜槽8が2槽並列に配設されているので、貯水タン
クを要せずとも中空糸膜槽8の中空糸膜9を浄水で逆洗
でき、これにより、常に使用者等に微細なゴミ等のない
浄水を供給できる。また、中空糸膜9の使用期間(又は
浄化期間)を長期化できる。
As described above, according to this embodiment, since the two hollow fiber membrane tanks 8 are arranged in parallel in the system, the hollow fiber membrane tank 8 does not require a water storage tank. 9 can be backwashed with purified water, whereby the user can always be supplied with purified water without fine dust. In addition, the usage period (or purification period) of the hollow fiber membrane 9 can be extended.

【0023】(実施例2)以下、本発明の第2実施例に
おける中空糸膜型浄水器について、図面を参照しながら
説明する。図6は本発明の第2実施例における中空糸膜
型浄水器及びその浄化状態を示す断面図、図7は本発明
の第2実施例における中空糸膜型浄水器及び二の中空糸
膜槽の逆洗状態を示す断面図、図8は本発明の第2実施
例における中空糸膜型浄水器及び一の中空糸膜槽の逆洗
状態を示す断面図、図9は本発明の第2実施例における
中空糸膜型浄水器,及び一の中空糸膜槽の逆洗状態と一
の中空糸膜槽の浄化状態を示す断面図である。2は原水
管、3は供給管、4は水栓、5は活性炭槽、6は活性
炭、7はフィルタ、9は中空糸膜であり、これらは従来
例と同様なものであり、同一の符号を付して説明を省略
する。1′は本発明の第2実施例における中空糸膜型浄
水器、81 ′,82 ′,83 ′は中空糸膜9,9,9を
備えた中空糸膜槽、10′は活性炭槽5と各中空糸膜槽
1 ′,82 ′,83 ′とを接続した給水分岐管、11
1 ′,112 ′,113 ′は給水分岐管10′の分岐部
に各々配設された給水弁、121 ′,122 ′,12
3 ′は給水分岐管10′の分岐部から各々分岐された洗
浄水排水管、131 ′,132 ′,133 ′は各洗浄水
排水管121 ′,122 ′,123 ′に配設された洗浄
水排水弁、141 ′,142 ′,143 ′は各中空糸膜
槽81 ′,82 ′,83 ′に各々接続された浄水吐水
管、15′は浄水吐水管141 ′,142 ′,143
を統合する、すなわち浄水吐水管141 ′,142 ′,
143 ′に各々分岐端が接続された統合吐水管、16
1 ′,162 ′,163 ′は浄水吐水管141 ′,14
2 ′,143 ′に各々配設された浄水吐水弁、17
1 ′,172 ′は各浄水吐水管同士(ここでは浄水吐水
管142 ′と浄水吐水管141 ′,及び浄水吐水管14
2 ′と浄水吐水管143 ′)を各々接続する浄水分岐
管、173 ′は各浄水吐水管同士(ここでは浄水吐水管
141 ′と浄水吐水管143 ′)を接続する他の浄水分
岐管、181 ′,182 ′は各浄水分岐管171 ′,1
2 ′に各々配設された浄水分岐弁、183 ′は他の浄
水分岐管173 ′に配設された他の浄水分岐弁である。
尚、浄水分岐管171 ′,172 ′及び他の浄水分岐管
173 ′を以下浄水分岐管171 ′,172 ′,17
3 ′と総称し、また浄水分岐弁18 1 ′,182 ′及び
他の浄水分岐弁183 ′も以下浄水分岐弁181 ′,1
2′,183 ′と総称するものとする。
(Embodiment 2) Hereinafter, a second embodiment of the present invention will be described.
Hollow fiber membrane type water purifier in
explain. FIG. 6 is a hollow fiber membrane according to the second embodiment of the present invention.
Type water purifier and a sectional view showing its purified state, FIG. 7 shows the present invention.
Hollow fiber membrane type water purifier and second hollow fiber in the second embodiment
Sectional drawing which shows the backwashing state of the membrane tank, FIG. 8 shows the second embodiment of the present invention.
Backwash of hollow fiber membrane water purifier and one hollow fiber membrane tank in example
FIG. 9 is a sectional view showing a state, and FIG. 9 shows a second embodiment of the present invention.
Hollow fiber membrane type water purifier and backwash state of one hollow fiber membrane tank
FIG. 3 is a cross-sectional view showing a purified state of the hollow fiber membrane tank. 2 is raw water
Pipe, 3 supply pipe, 4 faucet, 5 activated carbon tank, 6 activated
Charcoal, 7 is a filter, and 9 is a hollow fiber membrane.
It is similar to the example, and the same symbols are attached and explanations are omitted.
To do. Reference numeral 1'denotes a hollow fiber membrane type cleaner in the second embodiment of the present invention.
Water bottle, 81 ', 82 ', 83 ′ Is the hollow fiber membrane 9, 9, 9.
Hollow fiber membrane tank provided with 10 ', activated carbon tank 5 and each hollow fiber membrane tank
81 ', 82 ', 83 ′ And a water supply branch pipe connected to it, 11
1 ', 112 ', 113 ′ Is a branch portion of the water supply branch pipe 10 ′
Water supply valves, 121 ', 122 ', 12
3 ′ Is the washing water branched from each branch of the water supply branch pipe 10 ′.
Purified water drainage pipe, 131 ', 132 ', 133 ′ Is each wash water
Drainage pipe 121 ', 122 ', 123 Cleaning located in '
Water drain valve, 141 ', 142 ', 143 ′ Is each hollow fiber membrane
Tank 81 ', 82 ', 83 Purified water spout connected to each '
Pipe, 15 'is a clean water discharge pipe 141 ', 142 ', 143 ′
, That is, the clean water discharge pipe 141 ', 142 ′,
143 ′, An integrated water discharge pipe with branch ends connected to each, 16
1 ', 162 ', 163 ′ Is a clean water discharge pipe 141 ', 14
2 ', 143 ′, Each of the clean water discharge valves, 17
1 ', 172 ′ Is for each clean water discharge pipe (here
Tube 142 'And clean water discharge pipe 141 'And the clean water discharge pipe 14
2 'And clean water discharge pipe 143 ′) Water purification branch connecting each
Tube, 173 ′ Is for each clean water discharge pipe (here, clean water discharge pipe
141 'And clean water discharge pipe 143 ′) Other purified water connecting
Manifold, 181 ', 182 ′ Is each clean water branch pipe 171 ', 1
72 ′, Clean water branch valves, 183 ′ Is another purification
Water branch pipe 173 It is another clean water branch valve disposed in ′.
In addition, clean water branch pipe 171 ', 172 'And other clean water branch pipes
173 ′ Is the following purified water branch pipe 171 ', 172 ', 17
3 ’, And a water purifying branch valve 18 1 ', 182 'as well as
Other clean water branch valve 183 ′ Is also the clean water branch valve 181 ', 1
82', 183 Shall be collectively referred to as ′.

【0024】以上のように構成された本実施例の中空糸
膜型浄水器1について、以下その動作について説明す
る。まず、中空糸膜型浄水器1の浄化動作を説明する。
まず、水栓4,各給水弁111 ′,112 ′,113
及び各浄水吐水弁161 ′,162 ′,163 ′が
“開”とされ、また各洗浄水排水弁131 ′,13
2 ′,133′及び各浄水分岐弁181 ′,182 ′,
183 ′が“閉”とされる。次に、実施例1と同様にし
て、原水が原水管2から供給管3を介して活性炭槽5に
給水され、活性炭槽5で残留塩素やカルキ分等が取り除
かれる。次に、原水は、フィルタ7を通過し、その後、
図6中矢視するように、給水分岐管10′を介して各中
空糸膜槽81 ′,82 ′,83 ′に給水される。次に、
実施例1と同様にして、原水は、中空糸膜槽81 ′,8
2 ′,83 ′で微細なゴミや一般細菌が取り除かれる。
次に、中空糸膜槽81 ′,82 ′,83 ′で浄化された
浄水は、図6中矢視するように、浄水吐水管141 ′,
142 ′,143 ′及び統合吐水管15′を順次介して
使用者等に供給される。尚、本実施例では、全中空糸膜
槽81′,82 ′,83 ′で原水を浄化する場合につい
て説明したが、例えば三の中空糸膜槽81 ′,82 ′,
3 ′の内二の中空糸膜槽81 ′,82 ′で原水を浄化
したり、また一の中空糸膜槽81 ′で原水を浄化したり
してもよい。
The operation of the hollow fiber membrane water purifier 1 of the present embodiment having the above-described structure will be described below. First, the purification operation of the hollow fiber membrane water purifier 1 will be described.
First, the faucet 4, each water supply valve 11 1 ′, 11 2 ′, 11 3
And the clean water discharge valves 16 1 ′, 16 2 ′, 16 3 ′ are “open”, and the clean water discharge valves 13 1 ′, 13
2 ′, 13 3 ′ and each water purification branch valve 18 1 ′, 18 2 ′,
18 3 ′ is closed. Next, in the same manner as in Example 1, raw water is supplied from the raw water pipe 2 to the activated carbon tank 5 through the supply pipe 3, and residual chlorine, chlorine and the like are removed in the activated carbon tank 5. The raw water then passes through the filter 7, after which
As shown by the arrow in FIG. 6, water is supplied to each hollow fiber membrane tank 8 1 ′, 8 2 ′, 8 3 ′ via a water supply branch pipe 10 ′. next,
In the same manner as in Example 1, the raw water is the hollow fiber membrane tank 8 1 ′, 8
2 ', 8 3' fine dust and general bacteria are removed by.
Next, the purified water purified in the hollow fiber membrane tanks 8 1 ′, 8 2 ′, and 8 3 ′ is, as shown by the arrow in FIG. 6, purified water discharge pipes 14 1 ′,
It is supplied to the user or the like through 14 2 ′, 14 3 ′ and the integrated water discharge pipe 15 ′ in order. In this embodiment, the case where the raw water is purified by the all hollow fiber membrane tanks 8 1 ′, 8 2 ′ and 8 3 ′ has been described, but, for example, three hollow fiber membrane tanks 8 1 ′, 8 2 ′,
8 3 'hollow fiber membrane tank 81 among second of', 8 2 'or purify raw water, also one hollow fiber membrane tank 8 1' may or purifying raw water.

【0025】次に、中空糸膜型浄水器1の逆洗動作につ
いて説明する。まず、中空糸膜型浄水器1の内二の中空
糸膜槽の逆洗動作について説明する。ここでは、中空糸
膜槽82 ′,8 3′を逆洗する場合について説明する。
まず、水栓4,給水弁111 ′,洗浄水排水弁13
2 ′,133 ′及び浄水分岐弁18 1 ′,183 ′が
“開”とされ、また給水弁112 ′,113 ′,洗浄水
排水弁131 ′,各浄水吐水弁161 ′,162 ′,1
3 ′及び浄水分岐弁182 ′が“閉”とされる。次
に、前述の浄化動作と同様にして、原水が原水管2から
供給管3を介して活性炭槽5に給水された後、活性炭槽
5で残留塩素やカルキ分等が取り除かれる。次に、原水
は、フィルタ7を通過後、図7中矢視するように、給水
分岐管10′を介して中空糸膜槽81 ′に給水される。
次に、やはり前述の浄化動作と同様にして、原水は、中
空糸膜槽81 ′の中空糸膜9で微細なゴミや一般細菌が
取り除かれる。次に、図7中矢視するように、中空糸膜
槽81 ′で浄化された浄水は、浄水吐水管141 ′,浄
水分岐管171 ′及び浄水吐水管14 2 ′を順次介して
中空糸膜槽82 ′に給水される一方、浄水吐水管14
1 ′,浄水分岐管173 ′及び浄水吐水管143 ′を順
次介して中空糸膜槽83 ′に給水される。次に、浄水
は、実施例1と同様にして、中空糸膜槽82 ′,83
の中空糸膜9,9にトラップされた微細なゴミや一般細
菌を取り除く。次に、この中空糸膜槽82 ′,83 ′の
中空糸膜9,9を洗浄した洗浄水は、それぞれ洗浄水排
水管122 ′,123 ′を介して排水される。尚、本実
施例では、浄水分岐弁183 ′を“開”とした場合につ
いて説明したが、水圧等を制御できれば浄水分岐弁18
3 ′の代わりに浄水分岐弁182 ′を“開”としてもよ
く、また全浄水分岐弁181 ′,182 ′,183 ′を
“開”としてもよい。また、本実施例では、中空糸膜槽
2 ′,83 ′を逆洗する場合について説明したが、中
空糸膜槽82 ′,83 ′を逆洗する場合について説明し
たが、中空糸膜槽81 ′,82 ′や中空糸膜槽81 ′,
3 ′を逆洗する場合についても同様である。
Next, the backwash operation of the hollow fiber membrane water purifier 1 will be described.
And explain. First, two hollows in the hollow fiber membrane water purifier 1
The backwash operation of the yarn membrane tank will be described. Here the hollow fiber
Membrane tank 82 ', 83The case of backwashing ′ will be described.
First, the faucet 4 and the water supply valve 111 ′, Wash water drain valve 13
2 ', 133 ′ And clean water branch valve 18 1 ', 183 'But
“Open” and water supply valve 112 ', 113 ′, Wash water
Drain valve 131 ′ 、 Each clean water discharge valve 161 ', 162 ', 1
63 ′ And clean water branch valve 182 ′ Is “closed”. Next
In the same way as the above-mentioned purification operation, the raw water is fed from the raw water pipe 2.
After water is supplied to the activated carbon tank 5 through the supply pipe 3, the activated carbon tank
Residual chlorine and chlorine content are removed at 5. Next, raw water
After passing through the filter 7, as shown by the arrow in FIG.
Hollow fiber membrane tank 8 via branch pipe 10 '1 'Is supplied with water.
Next, the raw water is
Empty film tank 81 With the hollow fiber membrane 9 of ′, fine dust and general bacteria
To be removed. Next, as shown by the arrow in FIG. 7, a hollow fiber membrane
Tank 81 The purified water purified by ′ is the purified water discharge pipe 141 ′, Ji
Water branch pipe 171 'And the clean water discharge pipe 14 2 Through ’
Hollow fiber membrane tank 82 'While being supplied with water, the purified water discharge pipe 14
1 ′ 、 Purified water branch pipe 173 'And the clean water discharge pipe 143 ′ In order
Through the hollow fiber membrane tank 83 'Is supplied with water. Next, clean water
In the same manner as in Example 1, the hollow fiber membrane tank 82 ', 83 ′
Fine dust and general fine particles trapped in the hollow fiber membranes 9, 9 of
Remove the fungus. Next, this hollow fiber membrane tank 82 ', 83 'of
The washing water used to wash the hollow fiber membranes 9 and 9 is discharged respectively from the washing water.
Water pipe 122 ', 123 Drain through ′. In addition,
In the embodiment, the clean water branch valve 183 When ′ is set to “open”
However, if the water pressure etc. can be controlled, the water purification branch valve 18
3 Clean water branch valve 18 instead of '2 ′ May be “open”
Also, all clean water branch valve 181 ', 182 ', 183 ′
It may be "open". Further, in this example, the hollow fiber membrane tank
82 ', 83 I explained the case of backwashing '
Empty film tank 82 ', 83 Explain the case of backwashing
But, hollow fiber membrane tank 81 ', 82 'And hollow fiber membrane tank 81 ′,
83 The same applies to the case of backwashing ′.

【0026】次に、中空糸膜型浄水器1′の内一の中空
糸膜槽の逆洗動作について説明する。ここでは、中空糸
膜槽83 ′を逆洗する場合について説明する。まず、水
栓4,給水弁111 ′,112 ′,洗浄水排水弁13
3 ′及び浄水分岐弁182 ′,183 ′が“開”とさ
れ、また給水弁113 ′,洗浄水排水弁161 ′,16
2′,各浄水吐水弁161 ′,162 ′,163 ′及び
浄水分岐弁181 ′が“閉”とされる。次に、前述の浄
化動作と同様にして、原水が原水管2から供給管3を介
して活性炭槽5に給水された後、活性炭槽5で残留塩素
やカルキ分等が取り除かれる。次に、原水は、フィルタ
7を通過後、図8中矢視するように、給水分岐管10′
を介して中空糸膜槽81 ′,82 ′に給水される。次
に、やはり前述の浄化動作と同様にして、原水は、中空
糸膜槽81 ′,82 ′の中空糸膜9,9で微細なゴミや
一般細菌が取り除かれる。次に、図8中矢視するよう
に、中空糸膜槽81 ′で浄化された浄水は、浄水吐水管
141 ′,浄水分岐管173 ′及び浄水吐水管143
を順次介して中空糸膜槽83 ′に給水され、また中空糸
膜槽82 ′で浄化された浄水は、浄水吐水管142 ′,
浄水分岐管172 ′及び浄水吐水管143 ′を順次介し
て中空糸膜槽83 ′に給水される。次に、浄水は、やは
り前述の逆洗動作と同様にして、中空糸膜槽83 ′の中
空糸膜9にトラップされた微細なゴミや一般細菌を取り
除いた後、この中空糸膜槽83 ′の中空糸膜9を洗浄し
た洗浄水は、洗浄水排水管123 ′を介して排水され
る。尚、本実施例では、浄水分岐弁183 ′を“開”と
した場合について説明したが、浄水分岐弁183 ′の代
わりに浄水分岐弁181 ′を“開”としてもよく、また
全浄水分岐弁181 ′,182 ′,183 ′を“開”と
してもよい。また、本実施例では、中空糸膜槽83 ′を
逆洗する場合について説明したが、中空糸膜槽81 ′,
2′を逆洗する場合についても同様である。
Next, the backwashing operation of one hollow fiber membrane tank of the hollow fiber membrane water purifier 1'will be described. Here, the case where the hollow fiber membrane tank 8 3 ′ is backwashed will be described. First, the faucet 4, the water supply valves 11 1 ′ and 11 2 ′, the wash water drain valve 13
3 ′ and the clean water branch valves 18 2 ′ and 18 3 ′ are “open”, and the water supply valve 11 3 ′ and the wash water drain valves 16 1 ′ and 16
2 ′, each of the purified water discharge valves 16 1 ′, 16 2 ′, 16 3 ′ and the purified water branch valve 18 1 ′ are “closed”. Next, in the same manner as the above-described purification operation, raw water is supplied from the raw water pipe 2 to the activated carbon tank 5 through the supply pipe 3, and then the residual chlorine, the chlorine content and the like are removed in the activated carbon tank 5. Next, the raw water, after passing through the filter 7, as shown by the arrow in FIG.
Water is supplied to the hollow fiber membrane tanks 8 1 ′ and 8 2 ′ via the. Next, in the same manner as the above-mentioned purification operation, the raw water is subjected to removal of fine dust and general bacteria in the hollow fiber membranes 9 and 9 of the hollow fiber membrane tanks 8 1 ′ and 8 2 ′. Next, as shown by the arrow in FIG. 8, the purified water purified in the hollow fiber membrane tank 8 1 ′ is the purified water discharge pipe 14 1 ′, the purified water branch pipe 17 3 ′, and the purified water discharge pipe 14 3 ′.
The purified water, which is supplied to the hollow fiber membrane tank 8 3 ′ through the above and purified in the hollow fiber membrane tank 8 2 ′, is the purified water discharge pipe 14 2 ′,
Water is supplied to the hollow fiber membrane tank 8 3 ′ through the purified water branch pipe 17 2 ′ and the purified water discharge pipe 14 3 ′ in order. Next, in the purified water, fine dust and general bacteria trapped in the hollow fiber membrane 9 of the hollow fiber membrane tank 8 3 ′ are removed in the same manner as the above-mentioned backwashing operation, and then this hollow fiber membrane tank 8 3 The washing water for washing the 3'hollow fiber membrane 9 is drained through the washing water drain pipe 12 3 '. In addition, in this embodiment, the case where the purified water branch valve 18 3 ′ is “open” has been described, but the purified water branch valve 18 1 ′ may be “open” instead of the purified water branch valve 18 3 ′, or all of them may be opened. The clean water branch valves 18 1 ′, 18 2 ′ and 18 3 ′ may be “open”. In addition, although the case where the hollow fiber membrane tank 8 3 ′ is backwashed has been described in the present embodiment, the hollow fiber membrane tank 8 1 ′,
The same applies to the case of backwashing 8 2 ′.

【0027】次に、中空糸膜型浄水器1′の中空糸膜槽
の内一の中空糸膜槽の中空糸膜9を逆洗しかつ他の一の
中空糸膜槽で浄化する動作について説明する。ここで
は、中空糸膜槽82 ′を逆洗しかつ中空糸膜槽83 ′で
浄化する場合について説明する。まず、水栓4,給水弁
111 ′,113 ′,洗浄水排水弁132 ′,浄水吐水
弁163 ′及び浄水分岐弁181 ′が“開”とされ、ま
た給水弁112 ′,洗浄水排水弁131 ′,133 ′,
浄水吐水弁161 ′,162 ′及び浄水分岐弁18
2 ′,183 ′が“閉”とされる。次に、前述の浄化動
作と同様にして、原水が原水管2から供給管3を介して
活性炭槽5に給水された後、活性炭槽5で残留塩素やカ
ルキ分等が取り除かれる。次に、原水は、フィルタ7を
通過後、図9中矢視するように、給水分岐管10′を介
して中空糸膜槽81 ′,83 ′に給水される。次に、や
はり前述の浄化動作と同様にして、原水は、中空糸膜槽
1 ′,83 ′の中空糸膜9,9で微細なゴミや一般細
菌が取り除かれる。次に、図9中矢視するように、中空
糸膜槽81 ′で浄化された浄水は、浄水吐水管14
1 ′,浄水分岐管171 ′及び浄水吐水管142 ′を順
次介して中空糸膜槽82 ′に給水され、また中空糸膜槽
3 ′で浄化された浄水は、浄水吐水管143 ′,統合
吐水管15′を順次介して使用者等に供給される。次
に、中空糸膜槽82 ′に給水された浄水は、やはり前述
の逆洗動作と同様にして、中空糸膜槽82 ′の中空糸膜
9にトラップされた微細なゴミや一般細菌を取り除いた
後、洗浄水は、洗浄水排水管122 ′を介して排水され
る。尚、本実施例では、中空糸膜槽82 ′を逆洗しかつ
中空糸膜槽83 ′で浄化する場合について説明したが、
中空糸膜槽8 2 ′を逆洗しかつ中空糸膜槽81 ′で浄化
する場合や、また中空糸膜槽81 ′を逆洗しかつ中空糸
膜槽82 ′又は中空糸膜槽83 ′で浄化する場合,更に
中空糸膜槽83 ′を逆洗しかつ中空糸膜槽81 ′又は中
空糸膜槽82 ′で浄化する場合についても同様である。
Next, the hollow fiber membrane tank of the hollow fiber membrane water purifier 1 '
Backwash the hollow fiber membrane 9 in one of the hollow fiber membrane tanks and
The operation of purifying in the hollow fiber membrane tank will be described. here
Is a hollow fiber membrane tank 82 'Backwash and hollow fiber membrane tank 83 'so
The case of purification will be described. First, tap 4, water valve
111 ', 113 ′, Wash water drain valve 132 ′ 、 Clean water discharge
Valve 163 ′ And clean water branch valve 181 ′ Is “open”,
Water supply valve 112 ′, Wash water drain valve 131 ', 133 ′,
Clean water spout valve 161 ', 162 ′ And clean water branch valve 18
2 ', 183 ′ Is “closed”. Next, the purifying action described above
Raw water is fed from the raw water pipe 2 through the supply pipe 3 in the same manner as the production.
After water is supplied to the activated carbon tank 5, residual chlorine and carbon
Ruki etc. are removed. Next, for raw water, filter 7
After passing, as shown by the arrow in FIG.
And hollow fiber membrane tank 81 ', 83 'Is supplied with water. Then,
Beam In the same way as the above-mentioned purification operation, raw water is fed into the hollow fiber membrane tank.
81 ', 83 The ‘hollow fiber membranes 9 and 9’
The fungus is removed. Next, as shown by the arrow in FIG.
Thread film tank 81 The purified water purified by ′ is the purified water discharge pipe 14
1 ′ 、 Purified water branch pipe 171 'And the clean water discharge pipe 142 ′ In order
Through the hollow fiber membrane tank 82 'Is supplied with water, and is also a hollow fiber membrane tank
83 The purified water purified by ′ is the purified water discharge pipe 143 ′ 、 Integration
It is supplied to the user or the like through the water discharge pipe 15 'in sequence. Next
The hollow fiber membrane tank 82 The clean water supplied to the ‘
In the same manner as the backwashing operation of the hollow fiber membrane tank 82 ′ Hollow fiber membrane
Removed fine dust and general bacteria trapped in 9
After that, the washing water is washed water drain pipe 122 Drained through ′
It In the present embodiment, the hollow fiber membrane tank 82 Backwash and
Hollow fiber membrane tank 83 I explained the case of purifying with '
Hollow fiber membrane tank 8 2 'Backwash and hollow fiber membrane tank 81 Purify with ′
When you do, again hollow fiber membrane tank 81 'Backwash and hollow fiber
Membrane tank 82 ′ Or hollow fiber membrane tank 83 When purifying with '
Hollow fiber membrane tank 83 'Backwash and hollow fiber membrane tank 81 ′ Or medium
Empty film tank 82 The same applies to the case of purifying with ′.

【0028】以上のように本実施例によれば、系内に中
空糸膜槽が3槽並列に配設されているので、貯水タンク
を要せずとも中空糸膜槽の中空糸膜を浄水で逆洗でき、
これにより、常に使用者等に微細なゴミ等のない浄水を
供給できる。また、中空糸膜の使用期間(又は浄化期
間)を長期化できる。また、使用者に浄水を供給しつつ
中空糸膜の逆洗を行うことができ、この結果、逆洗時間
を必要とすることなく常に使用者に浄水を供給できる。
更に浄水分岐管に加え、浄水吐水管同士を接続する他の
浄水分岐管を備え、すなわち各浄水吐水管同士を接続す
る浄水分岐管を備えたので、各中空糸膜槽に水圧等の低
下等なく均一に浄水を供給することができる。尚、中空
糸膜槽は、2槽又は3槽に限らず、複数備えられてもよ
い。これにより、中空糸膜の使用期間(又は浄化期間)
を更に長期化でき、使用者等の利便性を向上でき、かつ
より一層浄化効果を向上できる。
As described above, according to this embodiment, since three hollow fiber membrane tanks are arranged in parallel in the system, the hollow fiber membranes in the hollow fiber membrane tank are purified without water storage tanks. Can be backwashed with
As a result, the user can always be supplied with purified water free from fine dust and the like. In addition, the usage period (or purification period) of the hollow fiber membrane can be extended. Moreover, the hollow fiber membrane can be backwashed while supplying purified water to the user, and as a result, purified water can be constantly supplied to the user without requiring backwashing time.
Furthermore, in addition to the purified water branch pipe, other purified water branch pipes that connect the purified water discharge pipes to each other, that is, the purified water branch pipe that connects the purified water discharge pipes to each other, so that the pressure of water in each hollow fiber membrane tank decreases It is possible to supply purified water evenly. The number of hollow fiber membrane tanks is not limited to two or three, and a plurality of hollow fiber membrane tanks may be provided. As a result, the usage period (or purification period) of the hollow fiber membrane
Can be further prolonged, convenience for users and the like can be improved, and the purification effect can be further improved.

【0029】[0029]

【発明の効果】以上のように本発明によれば、活性炭槽
と、中空糸膜槽と、を備えた中空糸膜型浄水器であっ
て、前記中空糸膜槽が、系内に並列に配設されているの
で、活性炭槽で残留塩素等が除去された原水に含まれる
微細なゴミや一般細菌等を複数の中空糸膜槽で除去でき
るので、浄化効果を高めることができ、かつ中空糸膜の
寿命(又は使用期間,浄化期間)を延命化(又は長期
化)できるので、常に微細なゴミや一般細菌等のない浄
水を供給でき、浄化効果等の信頼性に優れた小型の中空
糸膜型浄水器を実現できる。
As described above, according to the present invention, there is provided a hollow fiber membrane type water purifier comprising an activated carbon tank and a hollow fiber membrane tank, wherein the hollow fiber membrane tanks are arranged in parallel in the system. Since it is installed, it is possible to remove fine dust and general bacteria contained in raw water from which residual chlorine etc. has been removed in the activated carbon tank in multiple hollow fiber membrane tanks, so the purification effect can be enhanced and the hollow Since the life (or use period, purification period) of the fiber membrane can be extended (or extended), purified water that is always free of fine dust and general bacteria can be supplied, and a small hollow with excellent purification effect A thread film type water purifier can be realized.

【0030】また前記活性炭槽と前記各中空糸膜槽とを
接続する給水分岐管と、前記給水分岐管に各々配設され
る給水弁と、前記給水分岐管から各々分岐される洗浄水
排水管と、前記各洗浄水排水管に各々配設される洗浄水
排水弁と、前記各中空糸膜槽に各々接続される浄水吐水
管と、前記各浄水吐水管を統合する統合吐水管と、前記
統合吐水管に配設される浄水吐水弁と、を備えたので、
一方の中空糸膜槽で浄化された浄水を他方の中空糸膜槽
に供給できるので、中空糸膜槽の中空糸膜を浄水で洗浄
することができ、逆洗時に中空糸膜内に微細なゴミ等が
トラップされることがなく、常に微細なゴミや一般細菌
等のない浄水を供給でき、また貯水タンク等を不要とす
ることができ、浄化効果等の信頼性に優れた小型の中空
糸膜型浄水器を実現できる。
Further, a water supply branch pipe connecting the activated carbon tank and each of the hollow fiber membrane tanks, a water supply valve arranged in each of the water supply branch pipes, and a wash water drainage pipe branched from the water supply branch pipe. A wash water drain valve disposed in each of the wash water drain pipes, a clean water discharge pipe connected to each of the hollow fiber membrane tanks, and an integrated discharge pipe integrating the purified water discharge pipes, Since it has a purified water discharge valve arranged in the integrated discharge pipe,
Since the purified water purified in one hollow fiber membrane tank can be supplied to the other hollow fiber membrane tank, the hollow fiber membranes in the hollow fiber membrane tank can be washed with purified water, and fine particles are left inside the hollow fiber membrane during backwashing. A small hollow fiber that does not trap dust and can always supply purified water that does not contain fine dust or general bacteria, and that does not require a water storage tank, etc. A membrane water purifier can be realized.

【0031】また前記活性炭槽と前記各中空糸膜槽とを
接続する給水分岐管と、前記給水分岐管に各々配設され
る給水弁と、前記給水分岐管から各々分岐される洗浄水
排水管と、前記各洗浄水排水管に各々配設される洗浄水
排水弁と、前記各中空糸膜槽に各々接続される浄水吐水
管と、前記各浄水吐水管に配設される浄水吐水弁と、前
記各浄水吐水管同士を各々接続する浄水分岐管と、前記
各浄水分岐管に各々配設される浄水分岐弁と、前記各浄
水吐水管を統合する統合吐水管と、を備えたので、少な
くとも1の中空糸膜槽で浄化された浄水を他の中空糸膜
槽に供給できるので、中空糸膜槽の中空糸膜を浄水で洗
浄することができ、また中空糸膜槽の中空糸膜にトラッ
プされた微細なゴミ等のトラップ量によって浄化を行う
中空糸膜槽に供給する水量,水圧等を制御でき、中空糸
膜にトラップされた微細なゴミ等を確実に除去すること
ができ、常に微細なゴミや一般細菌等のない浄水を供給
でき、また貯水タンク等を不要とすることができ、浄化
効果等の信頼性に優れた小型の中空糸膜型浄水器を実現
できる。
Further, a water supply branch pipe connecting the activated carbon tank and each of the hollow fiber membrane tanks, a water supply valve provided in each of the water supply branch pipes, and a wash water drainage pipe branched from the water supply branch pipe. A wash water drain valve provided in each wash water drain pipe, a clean water discharge pipe connected to each hollow fiber membrane tank, and a clean water discharge valve provided in each clean water discharge pipe. , A purified water branch pipe connecting each of the purified water discharge pipes, a purified water branch valve disposed in each of the purified water branch pipes, and an integrated discharge pipe that integrates the purified water discharge pipes, Since purified water purified in at least one hollow fiber membrane tank can be supplied to another hollow fiber membrane tank, the hollow fiber membrane in the hollow fiber membrane tank can be washed with purified water, and the hollow fiber membrane in the hollow fiber membrane tank Supply to the hollow fiber membrane tank that purifies by the amount of trapped minute dust etc. The amount of water and water pressure that can be controlled can be controlled, the fine dust trapped in the hollow fiber membrane can be reliably removed, and purified water that is always free of fine dust and general bacteria can be supplied, and no water storage tank is required. Therefore, it is possible to realize a small-sized hollow fiber membrane water purifier having excellent reliability such as purification effect.

【0032】また前記各浄水吐水管同士を接続する他の
浄水分岐管と、前記他の浄水分岐管に配設される他の浄
水分岐弁と、を備えたので、逆洗時に一の中空糸膜槽で
浄化された浄水を他の二の中空糸膜槽に給水するとき
等、水圧等の低下等なく均一に浄水を供給することがで
き、逆洗時に中空糸膜槽に供給する浄水の水量,水圧等
をより的確に制御でき、これにより、より確実に中空糸
膜にトラップされた微細なゴミ等を除去でき、より一層
浄化効果を高めることができるので、信頼性に優れた小
型の中空糸膜型浄水器を実現できる。
Further, since the other purified water branch pipes connecting the respective purified water discharge pipes to each other and the other purified water branch valve arranged in the other purified water branch pipes are provided, one hollow fiber at the time of backwashing. When the purified water purified in the membrane tank is supplied to the other two hollow fiber membrane tanks, the purified water can be supplied uniformly without a decrease in water pressure, etc., and the purified water supplied to the hollow fiber membrane tank during backwashing. The amount of water, the water pressure, etc. can be controlled more accurately, and thus the fine dust and the like trapped in the hollow fiber membrane can be removed more reliably, and the purification effect can be further enhanced. A hollow fiber membrane type water purifier can be realized.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の第1実施例における中空糸膜型浄水器
及びその浄化状態を示す断面図
FIG. 1 is a cross-sectional view showing a hollow fiber membrane type water purifier and a purification state thereof in a first embodiment of the present invention.

【図2】本発明の第1実施例における中空糸膜型浄水器
及び一方の中空糸膜槽の逆洗状態を示す断面図
FIG. 2 is a sectional view showing a backwash state of the hollow fiber membrane type water purifier and one hollow fiber membrane tank in the first embodiment of the present invention.

【図3】本発明の第1実施例における中空糸膜型浄水器
及び他方の中空糸膜槽の逆洗状態を示す断面図
FIG. 3 is a sectional view showing a backwash state of the hollow fiber membrane type water purifier and the other hollow fiber membrane tank in the first embodiment of the present invention.

【図4】中空糸膜の浄化状態のメカニズムを示す断面図FIG. 4 is a cross-sectional view showing the mechanism of the purification state of the hollow fiber membrane.

【図5】中空糸膜の逆洗状態のメカニズムを示す断面図FIG. 5 is a cross-sectional view showing the mechanism of the backwash state of the hollow fiber membrane.

【図6】本発明の第2実施例における中空糸膜型浄水器
及びその浄化状態を示す断面図
FIG. 6 is a cross-sectional view showing a hollow fiber membrane type water purifier and a purification state thereof in a second embodiment of the present invention.

【図7】本発明の第2実施例における中空糸膜型浄水器
及び二の中空糸膜槽の逆洗状態を示す断面図
FIG. 7 is a sectional view showing a backwash state of the hollow fiber membrane type water purifier and the second hollow fiber membrane tank in the second embodiment of the present invention.

【図8】本発明の第2実施例における中空糸膜型浄水器
及び一の中空糸膜槽の逆洗状態を示す断面図
FIG. 8 is a sectional view showing a backwash state of the hollow fiber membrane type water purifier and one hollow fiber membrane tank in the second embodiment of the present invention.

【図9】本発明の第2実施例における中空糸膜型浄水
器,及び一の中空糸膜槽の逆洗状態と一の中空糸膜槽の
浄化状態を示す断面図
FIG. 9 is a cross-sectional view showing a hollow fiber membrane water purifier according to a second embodiment of the present invention, a backwash state of one hollow fiber membrane tank, and a purification state of one hollow fiber membrane tank.

【図10】従来の中空糸膜型浄水器及びその浄化状態を
示す断面図
FIG. 10 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its purified state.

【図11】従来の中空糸膜型浄水器及びその浄化状態を
示す断面図
FIG. 11 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its purification state.

【図12】従来の中空糸膜型浄水器及びその逆洗状態を
示す断面図
FIG. 12 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its backwashing state.

【図13】従来の中空糸膜型浄水器及びその浄化状態を
示す断面図
FIG. 13 is a cross-sectional view showing a conventional hollow fiber membrane water purifier and its purified state.

【図14】従来の中空糸膜型浄水器及びその逆洗状態を
示す断面図
FIG. 14 is a sectional view showing a conventional hollow fiber membrane water purifier and its backwashing state.

【符号の説明】[Explanation of symbols]

1,1′,1A,1A′,1A″ 中空糸膜型浄水器 2 原水管 3 供給管 4 水栓 5 活性炭槽 6 活性炭 7 フィルタ 81 ,82 ,81 ′,82 ′,83 ′,8A 中空糸膜
槽 9 中空糸膜 10,10′ 給水分岐管 111 ,112 ,111 ′,112 ′,113 ′ 給水
弁 11A 原水分岐管 121 ,122 ,121 ′,122 ′,123 ′,15
A 洗浄水排水管 12A 切替弁 12B 貯水タンク 131 ,132 ,131 ′,132 ′,133 ′,16
A 洗浄水排水弁 13A 供給弁 13B パワーピストン 141 ,142 ,141 ′,142 ′,143 ′,10
A 浄水吐水管 15,15′ 統合吐水管 16,161 ′,162 ′,163 ′,14A 浄水吐
水弁 171 ′,172 ′,173 ′,11B 浄水分岐管 181 ′,182 ′,183 ′ 浄水分岐弁
1,1 ', 1A, 1A', 1A "Hollow fiber membrane type water purifier 2 Raw water pipe 3 Supply pipe 4 Water faucet 5 Activated carbon tank 6 Activated carbon 7 Filter 8 1 , 8 2 , 8 1 ′, 8 2 ′, 8 3 ′, 8A Hollow fiber membrane tank 9 Hollow fiber membrane 10,10 ′ Water supply branch pipe 11 1 , 11 2 , 11 1 ′, 11 2 ′, 11 3 ′ Water supply valve 11A Raw water branch pipe 12 1 , 12 2 , 12 1 ′ , 12 2 ′, 12 3 ′, 15
A Wash water drain pipe 12A Switching valve 12B Water storage tank 13 1 , 13 2 , 13 1 ′, 13 2 ′, 13 3 ′, 16
A Wash water drain valve 13A Supply valve 13B Power piston 14 1 , 14 2 , 14 1 ′, 14 2 ′, 14 3 ′, 10
A Purified water discharge pipe 15, 15 'Integrated discharge pipe 16, 16 1 ', 16 2 ', 16 3 ', 14A Purified water discharge valve 17 1 ', 17 2 ', 17 3 ', 11B Purified water branch pipe 18 1 ', 18 2 ', 18 3' purified water branch valve

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】活性炭槽と、中空糸膜槽と、を備えた中空
糸膜型浄水器であって、前記中空糸膜槽が、系内に並列
に配設されていることを特徴とする中空糸膜型浄水器。
1. A hollow fiber membrane type water purifier comprising an activated carbon tank and a hollow fiber membrane tank, wherein the hollow fiber membrane tanks are arranged in parallel in a system. Hollow fiber membrane type water purifier.
【請求項2】請求項1に記載の中空糸膜型浄水器が、前
記活性炭槽と前記各中空糸膜槽とを接続する給水分岐管
と、前記給水分岐管に各々配設される給水弁と、前記給
水分岐管から各々分岐される洗浄水排水管と、前記各洗
浄水排水管に各々配設される洗浄水排水弁と、前記各中
空糸膜槽に各々接続される浄水吐水管と、前記各浄水吐
水管を統合する統合吐水管と、前記統合吐水管に配設さ
れる浄水吐水弁と、を備えたことを特徴とする中空糸膜
型浄水器。
2. The hollow fiber membrane-type water purifier according to claim 1, wherein a water supply branch pipe connecting the activated carbon tank and each of the hollow fiber membrane tanks, and a water supply valve arranged in each of the water supply branch pipes. A wash water drain pipe branched from each of the water supply branch pipes, a wash water drain valve provided in each wash water drain pipe, and a clean water discharge pipe connected to each hollow fiber membrane tank. A hollow fiber membrane type water purifier comprising: an integrated water discharge pipe that integrates the respective purified water discharge pipes; and a purified water discharge valve disposed in the integrated water discharge pipe.
【請求項3】請求項1に記載の中空糸膜型浄水器が、前
記活性炭槽と前記各中空糸膜槽とを接続する給水分岐管
と、前記給水分岐管に各々配設される給水弁と、前記給
水分岐管から各々分岐される洗浄水排水管と、前記各洗
浄水排水管に各々配設される洗浄水排水弁と、前記各中
空糸膜槽に各々接続される浄水吐水管と、前記各浄水吐
水管に配設される浄水吐水弁と、前記各浄水吐水管同士
を各々接続する浄水分岐管と、前記各浄水分岐管に各々
配設される浄水分岐弁と、前記各浄水吐水管を統合する
統合吐水管と、を備えたことを特徴とする中空糸膜型浄
水器。
3. The hollow fiber membrane type water purifier according to claim 1, wherein a water supply branch pipe connecting the activated carbon tank and each of the hollow fiber membrane tanks, and a water supply valve provided in each of the water supply branch pipes. A wash water drain pipe branched from each of the water supply branch pipes, a wash water drain valve provided in each wash water drain pipe, and a clean water discharge pipe connected to each hollow fiber membrane tank. , A purified water discharge valve arranged in each of the purified water discharge pipes, a purified water branch pipe connecting each of the purified water discharge pipes, a purified water branch valve arranged in each of the purified water branch pipes, and each of the purified water A hollow fiber membrane type water purifier, comprising: an integrated water discharge pipe that integrates the water discharge pipe.
【請求項4】請求項3に記載の中空糸膜型浄水器が、前
記各浄水吐水管同士を接続する他の浄水分岐管と、前記
他の浄水分岐管に配設される他の浄水分岐弁と、を備え
たことを特徴とする中空糸膜型浄水器。
4. The hollow fiber membrane type water purifier according to claim 3, wherein another purified water branch pipe for connecting the purified water discharge pipes to each other and another purified water branch disposed in the other purified water branch pipes. A hollow fiber membrane type water purifier characterized by having a valve.
JP6221314A 1994-09-16 1994-09-16 Hollow yarn membrane type water purifier Pending JPH0884989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6221314A JPH0884989A (en) 1994-09-16 1994-09-16 Hollow yarn membrane type water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6221314A JPH0884989A (en) 1994-09-16 1994-09-16 Hollow yarn membrane type water purifier

Publications (1)

Publication Number Publication Date
JPH0884989A true JPH0884989A (en) 1996-04-02

Family

ID=16764864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6221314A Pending JPH0884989A (en) 1994-09-16 1994-09-16 Hollow yarn membrane type water purifier

Country Status (1)

Country Link
JP (1) JPH0884989A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1009457C2 (en) * 1998-06-19 1999-12-21 Sepeq B V Apparatus and method for filtering a liquid.
WO2013011743A1 (en) * 2011-07-20 2013-01-24 シャープ株式会社 Water purifier
JP2013223866A (en) * 2013-06-12 2013-10-31 Mitsubishi Rayon Co Ltd Water purifier and method for cleaning the same
CN104014192A (en) * 2014-06-16 2014-09-03 芜湖市华泰实业有限公司 Simple and convenient water purifying filter element device
CN114588783A (en) * 2022-03-21 2022-06-07 山东水利建设集团有限公司巨野分公司 Multistage back flush system in pump house

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1009457C2 (en) * 1998-06-19 1999-12-21 Sepeq B V Apparatus and method for filtering a liquid.
EP0965377A1 (en) * 1998-06-19 1999-12-22 SepeQ B.V. Device for filtering a liquid and method for disinfecting such a device
US6203714B1 (en) 1998-06-19 2001-03-20 Sepeq B.V. Device for filtering a liquid and method for disinfecting such a device
WO2013011743A1 (en) * 2011-07-20 2013-01-24 シャープ株式会社 Water purifier
JP2013022506A (en) * 2011-07-20 2013-02-04 Sharp Corp Water purifier
CN103687814A (en) * 2011-07-20 2014-03-26 夏普株式会社 Water purifier
CN103687814B (en) * 2011-07-20 2016-06-29 夏普株式会社 Water purifier
US9669336B2 (en) 2011-07-20 2017-06-06 Sharp Kabushiki Kaisha Water purifier
JP2013223866A (en) * 2013-06-12 2013-10-31 Mitsubishi Rayon Co Ltd Water purifier and method for cleaning the same
CN104014192A (en) * 2014-06-16 2014-09-03 芜湖市华泰实业有限公司 Simple and convenient water purifying filter element device
CN114588783A (en) * 2022-03-21 2022-06-07 山东水利建设集团有限公司巨野分公司 Multistage back flush system in pump house
CN114588783B (en) * 2022-03-21 2023-08-01 山东水利建设集团有限公司 Multistage back flush system of pump house

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