JPH019573Y2 - - Google Patents

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Publication number
JPH019573Y2
JPH019573Y2 JP3984786U JP3984786U JPH019573Y2 JP H019573 Y2 JPH019573 Y2 JP H019573Y2 JP 3984786 U JP3984786 U JP 3984786U JP 3984786 U JP3984786 U JP 3984786U JP H019573 Y2 JPH019573 Y2 JP H019573Y2
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JP
Japan
Prior art keywords
dialysate
pump
water supply
valve
negative pressure
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
Application number
JP3984786U
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Japanese (ja)
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JPS61163654U (en
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Priority to JP3984786U priority Critical patent/JPH019573Y2/ja
Publication of JPS61163654U publication Critical patent/JPS61163654U/ja
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Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、陰圧型人工透析装置に関し、殊に熱
湯を循環供給して透析液供給系内を消毒するよう
に構成したものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a negative pressure type artificial dialysis device, and is particularly configured to circulate and supply hot water to disinfect the inside of the dialysate supply system.

〔従来の技術およびその問題点〕[Conventional technology and its problems]

陰圧型人工透析装置は、透析膜を介して血液中
の老廃物(たとえば、尿素やクレアチニンのよう
な蛋白代謝終末物質)および人体に有害な毒物や
薬物を潅流透析液に移行せしめて除去する際、潅
流透析側に常に一定の陰圧をかけて透析を行うよ
う構成したものである。
Negative pressure dialysis equipment removes waste products (e.g. protein metabolic end substances such as urea and creatinine) in the blood and poisons and drugs harmful to the human body by transferring them to the perfused dialysate through a dialysis membrane. , which is configured to perform dialysis by constantly applying a constant negative pressure to the perfusion dialysis side.

従来、この種の陰圧型人工透析装置を洗滌およ
び消毒するに際しては、熱水を使用し、この熱水
を透析回路中に1回通過させたのみで廃棄してし
まうのが常法であつた。
Conventionally, when cleaning and disinfecting this type of negative-pressure artificial dialysis machine, the conventional method was to use hot water, and to discard the hot water after passing it through the dialysis circuit once. .

しかしながら、このような消毒方法では熱水が
1回通過のみで廃棄されるため、完全な消毒を達
成するのに大量の熱水を必要とし、その熱水を得
るには多大の熱エネルギーが必要とされるので、
熱経済上損失が多くなる欠点がある。
However, these disinfection methods require a large amount of hot water to achieve complete disinfection, as the hot water is discarded after only one pass, and a large amount of thermal energy is required to obtain the hot water. Therefore,
The disadvantage is that there is a lot of heat-economic loss.

また、従来この種の人工透析装置において、透
析液流路の滅菌手段として、水を導入して流路の
入口と排液口とを相互に連結し、ヒーターにより
加熱した熱水により滅菌を行う閉鎖系を構成した
ものが提案されている(特開昭51−65467号公
報)。しかしながら、前記従来装置は、透析器に
対しその上流側と下流側にそれぞれポンプを設
け、上流側のポンプは透析液に所定の正圧を与
え、また下流側のポンプは透析液の負圧吸引と脱
気装置の吸引ポンプとして作用するよう構成し、
しかも滅菌時において作動させる専用のヒーター
を別個に設け、さらに透析モードから滅菌モード
に切換えるために水供給口と原液供給口と排水口
との接続を切換える切換弁を設けたものであり、
構成が極めて複雑であり、操作も煩雑になる難点
がある。
Conventionally, in this type of artificial dialysis machine, as a means of sterilizing the dialysate flow path, water is introduced, the inlet of the flow path and the drain port are interconnected, and sterilization is performed using hot water heated by a heater. A closed system configuration has been proposed (Japanese Unexamined Patent Publication No. 51-65467). However, in the conventional device, pumps are provided on the upstream and downstream sides of the dialyzer, and the pump on the upstream side applies a predetermined positive pressure to the dialysate, and the pump on the downstream side draws negative pressure from the dialysate. and configured to act as a suction pump for the deaerator,
Furthermore, a dedicated heater is separately provided to operate during sterilization, and a switching valve is provided to switch the connections between the water supply port, stock solution supply port, and drain port in order to switch from dialysis mode to sterilization mode.
The disadvantage is that the configuration is extremely complicated and the operation is complicated.

そこで、本考案者等は種々検討を重ねた結果、
希釈用水供給系に設けた加熱手段の入口側に陰圧
ポンプより吐出される加熱排水の排水系より分岐
する循環パイプを接続し、この循環パイプに開閉
弁を設け、洗滌時および消毒時に透析液原液およ
び希釈用水の供給を停止して前記開閉弁を開放す
るだけで、簡便に透析液供給系に加熱水を循環さ
せることができ、前述した従来装置の問題点を解
決することができることを突き止めた。
Therefore, as a result of various studies, the inventors of the present invention found that
A circulation pipe branching from the drainage system for heated wastewater discharged from a negative pressure pump is connected to the inlet side of the heating means installed in the dilution water supply system, and an on-off valve is installed in this circulation pipe to prevent dialysate during cleaning and disinfection. We discovered that by simply stopping the supply of stock solution and dilution water and opening the on-off valve, heated water can be easily circulated through the dialysate supply system, solving the problems of the conventional device described above. Ta.

従つて、本考案の目的は、透析時および洗滌時
に希釈用水供給系に設けた加熱手段を共用して透
析液供給系内の洗滌を簡便に行うことができる、
簡単な構成で操作の容易な陰圧型人工透析装置を
提供するにある。
Therefore, an object of the present invention is to easily wash the dialysate supply system by sharing the heating means provided in the dilution water supply system during dialysis and washing.
The purpose of the present invention is to provide a negative pressure type artificial dialysis device that has a simple configuration and is easy to operate.

〔問題点を解決するための手段〕[Means for solving problems]

前記の目的を達成するため、本考案に係る陰圧
型人工透析装置は、透析液原液と予め加熱手段3
6により適温に加熱した希釈用水とを混合して所
定濃度の透析液を得、この透析液を透析器10の
前に設置した脱気用の陰圧ポンプ42を経て、透
析器10の出口側に設けた陰圧ポンプ58の作用
下に透析液供給系88を介して透析器10に供給
するよう構成し、さらに前記透析液供給系88に
接続される透析器10の接続端子間に自動開閉弁
72を備えたバイパス管70で短絡してなる陰圧
型人工透析装置であつて、希釈用水供給系24に
設けた加熱手段36の入口側に、前記バイパス管
70を介して透析液を流過せしめ、前記陰圧ポン
プ58より吐出される排液を分岐するための循環
パイプ74を分岐すると共に、排液系62ならび
に該循環パイプ74のそれぞれに自動開閉弁6
0,76を設け、洗滌時および消毒時には透析液
原液および希釈用水の比例ポンプ18,32を停
止し、自動開閉弁54を閉塞し、同時に自動開閉
弁60を閉塞、自動開閉弁76を開放することに
よつて、密閉回路90を形成せしめ、該密閉回路
90内に加熱水を循環させることができるよう構
成することを特徴とする。
In order to achieve the above object, the negative pressure type artificial dialysis apparatus according to the present invention is provided with a heating means 3 in advance of the dialysate stock solution and
The dialysate is mixed with dilution water heated to an appropriate temperature in step 6 to obtain a dialysate of a predetermined concentration, and this dialysate is passed through a negative pressure pump 42 for degassing installed in front of the dialyzer 10 to the outlet side of the dialyzer 10. The dialysate is supplied to the dialyzer 10 via a dialysate supply system 88 under the action of a negative pressure pump 58 provided at This is a negative pressure type artificial dialysis device which is short-circuited by a bypass pipe 70 equipped with a valve 72, and the dialysate is passed through the bypass pipe 70 to the inlet side of the heating means 36 provided in the dilution water supply system 24. In addition, a circulation pipe 74 for branching the drained liquid discharged from the negative pressure pump 58 is branched, and an automatic on-off valve 6 is installed in each of the drain system 62 and the circulation pipe 74.
During cleaning and disinfection, the proportional pumps 18 and 32 of the dialysate stock solution and dilution water are stopped, the automatic on-off valve 54 is closed, the automatic on-off valve 60 is simultaneously closed, and the automatic on-off valve 76 is opened. Particularly, a closed circuit 90 is formed, and heated water can be circulated within the closed circuit 90.

本考案装置において、消毒操作時に密閉された
循環回路を構成して熱湯に循環させるに際し、蒸
発消失した熱湯量に相当する水量は、回路中に自
動的に補給されるよう構成される。
In the device of the present invention, when a closed circulation circuit is configured to circulate hot water during a disinfection operation, an amount of water corresponding to the amount of hot water lost by evaporation is automatically replenished into the circuit.

この場合、熱交換器を供給水加熱モータの上流
に付設し、この熱交換器において補給水を循環熱
水と熱交換させることにより予備加熱するのが熱
経済上好ましい。
In this case, it is preferable in terms of thermoeconomics that a heat exchanger is attached upstream of the feed water heating motor, and that the make-up water is preheated by exchanging heat with circulating hot water in this heat exchanger.

本考案装置において、蒸発熱湯相当量の水を補
給するに際しては、後述する特殊な比例ポンプと
して、次の3種の具体的手段を採用することがで
きる。
In the device of the present invention, when replenishing water equivalent to evaporated hot water, the following three types of specific means can be employed as a special proportional pump, which will be described later.

1 自給式ポンプを使用する。1 Use a self-contained pump.

2 一般給水ポンプとチエツク弁とを直列接続し
て使用し、このポンプに開閉弁を有するバイパ
ス管を接続する。
2. A general water supply pump and a check valve are connected in series, and a bypass pipe with an on-off valve is connected to this pump.

3 一般給水ポンプを使用し、このポンプに開閉
弁とチエツク弁とを直列接続したバイパス管を
接続する。
3 Use a general water supply pump and connect a bypass pipe with an on-off valve and a check valve connected in series to this pump.

これらの手段のうち、開閉弁と一般給水ポンプ
とを使用する場合、熱湯消毒時には弁を開放しか
つポンプを停止して補給水を水道圧により供給
し、逆止弁により循環熱水の逆流を阻止すること
ができる。
Among these means, when using an on-off valve and a general water supply pump, when disinfecting with boiling water, the valve is opened and the pump is stopped to supply make-up water using water pressure, and a check valve prevents the backflow of circulating hot water. can be prevented.

〔実施例〕〔Example〕

次に、本考案に係る陰圧型人工透析装置の実施
例につき添付図面を参照しながら以下詳細に説明
する。
Next, embodiments of the negative pressure type artificial dialysis apparatus according to the present invention will be described in detail below with reference to the accompanying drawings.

第1図において、参照符号10は透析器を示
し、この透析器としては透析液側に負圧をかけて
用いる陰圧型のものが使用される。まず、透析時
においては、透析液原液タンク12に貯留した透
析液原液の一定量が原液チヤンバ14、瀘過器1
6を介して比例供給ポンプ18により原液供給系
20内に給送され、さらに逆止弁22を経て希釈
用水供給系24と合流して所定濃度の透析液に希
釈するよう構成される。一方、希釈用水供給系2
4には、水供給源(図示せず)から自動弁26、
減圧弁28、圧力計30および比例ポンプ32を
介して希釈用水が供給され、さらにこの希釈用水
は熱交換器34および加熱手段としてのヒータ3
6によつて加温された後、前記の透析液原液と比
例混合される。透析液原液と希釈用水との比例混
合は比例ポンプ18,32によつて達成され、そ
の具体的手段として、例えば本出願人の特許出願
に係る特公昭59−39170号公報に開示された比例
供給ポンプを好適に使用することができる。希釈
された透析液(以下、単に透析液と云う)は、弁
38、脱気室40、陰圧ポンプ42およびガス抜
き装置44からなる循環系に供給し、透析液の滞
留を防止し、しかもその一部はガス抜き装置44
を経て濃度計46により濃度チエツクした後、完
全弁48、手動弁50、流量計52、自動開閉弁
54を介して透析器10中に導入される。透析器
10において血液中の老廃物を吸収した透析液は
圧力計56を経て陰圧ポンプ58により移送さ
れ、熱交換器34および自動開閉弁60を経て排
液系(以下、排水系62と称する)に排水され
る。なお透析器10内を負圧に保持する方法とし
て本出願人の特許出願に係る特開昭52−81997号
公報に開示された自動調圧弁64を用いた透析液圧
力調整装置が好適に使用される。また、希釈用水
供給系24のヒータ出口側および透析液供給系8
8の適所に夫々温度計68を設けて適宜透析液の
温度チエツクを行うよう構成する。
In FIG. 1, reference numeral 10 indicates a dialyzer, and this dialyzer is of a negative pressure type in which negative pressure is applied to the dialysate side. First, during dialysis, a certain amount of the dialysate concentrate stored in the dialysate concentrate tank 12 is transferred to the concentrate chamber 14 and the filter 1.
6 into the stock solution supply system 20 by the proportional supply pump 18, and further passes through the check valve 22 and joins the dilution water supply system 24 to be diluted to a dialysate of a predetermined concentration. On the other hand, dilution water supply system 2
4, an automatic valve 26 from a water supply (not shown);
Dilution water is supplied via a pressure reducing valve 28, a pressure gauge 30, and a proportional pump 32, and this dilution water is further supplied to a heat exchanger 34 and a heater 3 as a heating means.
6 and then proportionally mixed with the dialysate stock solution. Proportional mixing of the dialysate stock solution and dilution water is achieved by proportional pumps 18 and 32, and specific means thereof include, for example, the proportional supply method disclosed in Japanese Patent Publication No. 59-39170, which is filed by the present applicant. A pump can be suitably used. The diluted dialysate (hereinafter simply referred to as dialysate) is supplied to a circulatory system consisting of a valve 38, a degassing chamber 40, a negative pressure pump 42, and a gas venting device 44 to prevent stagnation of the dialysate and to Part of it is the gas venting device 44
After the concentration is checked by a concentration meter 46, it is introduced into the dialyzer 10 via a complete valve 48, a manual valve 50, a flow meter 52, and an automatic opening/closing valve 54. The dialysate that has absorbed waste products from the blood in the dialyzer 10 is transferred by a negative pressure pump 58 through a pressure gauge 56, and then passed through a heat exchanger 34 and an automatic shut-off valve 60 to a drainage system (hereinafter referred to as a drainage system 62). ) is drained. As a method for maintaining the inside of the dialyzer 10 at negative pressure, a dialysate pressure regulating device using an automatic pressure regulating valve 64 disclosed in Japanese Patent Application Laid-Open No. 52-81997 related to the patent application filed by the present applicant is preferably used. Ru. Also, the heater outlet side of the dilution water supply system 24 and the dialysate supply system 8
Thermometers 68 are provided at appropriate locations in each of the dialysers 8 to check the temperature of the dialysate as needed.

上述の如く構成した陰圧型人工透析装置におい
て、透析液供給系88に接続される透析器10の
接続端子間を短絡するバイパス管70を配設して
このバイパス管70に自動開閉弁72を接続し、
さらに排水系62の一部より希釈用水供給系24
のヒータ36の入口側へ連通する循環パイプ74
を配設してこの循環パイプ74に開閉弁76を接
続し、これらの自動開閉弁72,76は夫々透析
操作時において閉塞させておく。
In the negative pressure artificial dialysis apparatus configured as described above, a bypass pipe 70 is provided to short-circuit the connection terminals of the dialyzer 10 connected to the dialysate supply system 88, and an automatic on-off valve 72 is connected to the bypass pipe 70. death,
Further, from a part of the drainage system 62, the dilution water supply system 24
A circulation pipe 74 communicating with the inlet side of the heater 36
An on-off valve 76 is connected to the circulation pipe 74, and these automatic on-off valves 72 and 76 are kept closed during the dialysis operation.

次に、以上の構成からなる陰圧型人工透析装置
において、透析液供給系88を洗滌および消毒す
る場合について説明する。
Next, a case will be described in which the dialysate supply system 88 is cleaned and disinfected in the negative pressure type artificial dialysis apparatus having the above configuration.

洗滌操作では三方切換弁86を切換え比例ポン
プ18の原液側を希釈用水で洗滌すると共に、こ
の比例ポンプ18から吐出された希釈用水で配管
内を洗滌する。
In the washing operation, the three-way switching valve 86 is switched to wash the undiluted solution side of the proportional pump 18 with dilution water, and the inside of the piping is also washed with the dilution water discharged from the proportional pump 18.

次に、消毒操作では、消毒操作に先立ち、まず
原液供給系20のポンプ18の駆動を停止して原
液の供給を停止し、透析液供給系88の透析器1
0をはずし、バイパス管70を接続した後、前段
に設けた弁50を開放すると共に排水系62の弁
60を閉塞する。次いで、透析器10の接続端子
側を短絡するバイパス管70の自動開閉弁72を
開放すると共に排水系62と希釈用水供給系24
とを連通する循環パイプ74の自動開閉弁76を
開放する。このように操作することにより、加熱
された希釈用水は透析液供給系88内を循環する
こととなる。この場合、希釈用水供給系24に
は、給水源として水道水を利用した場合には、透
析液供給系88側に対し水道圧のみによつて自動
的に給水もしくは補給が行われるよう構成する。
このようにして、加熱循環水の蒸発熱湯相当量の
水が透析液供給系88内に補給される。
Next, in the disinfection operation, prior to the disinfection operation, first the drive of the pump 18 of the stock solution supply system 20 is stopped to stop the supply of stock solution, and the dialyzer 1 of the dialysate supply system 88 is stopped.
0 and connect the bypass pipe 70, the valve 50 provided in the previous stage is opened and the valve 60 of the drainage system 62 is closed. Next, the automatic opening/closing valve 72 of the bypass pipe 70 that short-circuits the connection terminal side of the dialyzer 10 is opened, and the drainage system 62 and dilution water supply system 24 are opened.
The automatic opening/closing valve 76 of the circulation pipe 74 that communicates with the station is opened. By operating in this manner, the heated dilution water is circulated within the dialysate supply system 88. In this case, the dilution water supply system 24 is configured so that when tap water is used as a water supply source, water is automatically supplied or replenished to the dialysate supply system 88 only by tap pressure.
In this way, the dialysate supply system 88 is replenished with an amount of water equivalent to the evaporated hot water of the heated circulating water.

なお、消毒操作時において、透析液供給系88
内に適宜水の補給を行うため、希釈用水供給系2
4に接続する比例ポンプ32としては、自給式ポ
ンプが好適に使用されるが。代案として、第2図
に示すように希釈用水供給系24に一般の遠心形
給水ポンプ78をその吐出側にチエツク弁80を
接続して使用することができる。この場合、給水
ポンプ78の吸込側と吐出側の間に自動開閉弁8
4を有するバイパス管82を接続し、前記ポンプ
の吐出側のバイパス管接続部の下流にチエツク弁
を接続し、消毒操作時において前記自動開閉弁8
4を開放するように構成することができる。
In addition, during the disinfection operation, the dialysate supply system 88
In order to replenish water appropriately, dilution water supply system 2 is installed.
As the proportional pump 32 connected to 4, a self-contained pump is preferably used. Alternatively, as shown in FIG. 2, a general centrifugal water pump 78 can be used in the dilution water supply system 24 with a check valve 80 connected to its discharge side. In this case, an automatic on-off valve 8 is installed between the suction side and the discharge side of the water supply pump 78.
A check valve is connected downstream of the bypass pipe connection part on the discharge side of the pump, and the automatic opening/closing valve 8 is connected during disinfection operation.
4 can be configured to be open.

また、別の代案として第3図に示すように、希
釈用水供給系24に一般の遠心形給水ポンプ78
を使用し、この給水ポンプ78の吸込側と吐出側
間に自動開閉弁84とチエツク弁80とを直列接
続してなるバイパス管82を接続して、前記と同
様に消毒操作時に自動開閉弁84を開放するよう
に構成することもできる。
As another alternative, as shown in FIG.
A bypass pipe 82 consisting of an automatic on-off valve 84 and a check valve 80 connected in series is connected between the suction side and the discharge side of this water supply pump 78, and the automatic on-off valve 84 is connected during the disinfection operation in the same way as described above. It can also be configured to open.

なお、消毒操作時において、第1図中点線で示
される密閉回路90を構成した透析液供給系88
内を流れる循環水の熱湯温度は、通常83〜92℃に
設定され、好ましくは87〜90℃である。また、熱
湯の蒸発に伴う循環水の減少を補給する補給水
は、熱交換器34において効果的に予熱される。
In addition, during the disinfection operation, the dialysate supply system 88 that constitutes the closed circuit 90 shown by the dotted line in FIG.
The temperature of the circulating water flowing inside is usually set at 83-92°C, preferably 87-90°C. Furthermore, makeup water that replenishes the decrease in circulating water due to evaporation of hot water is effectively preheated in the heat exchanger 34.

この場合、密閉回路90では一部加熱水が蒸発
するが、この分は比例ポンプ18,32が停止し
ても給水圧で補充することができる。
In this case, a portion of the heated water evaporates in the closed circuit 90, but this amount can be replenished by the water supply pressure even if the proportional pumps 18, 32 are stopped.

このようにして、熱湯消毒後は、適宜弁の開閉
操作を行つて透析液供給系88内の熱湯を全て廃
棄し、しかる後最初に述べた透析操作回路を構成
し、比例ポンプ18,32を駆動することによ
り、人工透析が再開される。
In this way, after boiling water disinfection, all the hot water in the dialysate supply system 88 is discarded by opening and closing the valves as appropriate, and then the dialysis operation circuit mentioned above is constructed and the proportional pumps 18, 32 are operated. By driving, artificial dialysis is restarted.

〔考案の効果〕[Effect of idea]

前述した実施例から明らかなように、本考案装
置によれば、透析液原液と予め加熱手段36によ
り適温に加熱した希釈用水とを混合して得た所定
濃度の透析液を得、この透析液を透析器10の前
に設置した脱気用の陰圧ポンプ42を経て、透析
液を透析器10の出口側に設けた陰圧ポンプ58
の作用下に透析液供給系88を介して透析器10
に供給するよう構成し、さらに前記透析液供給系
88に接続される透析器10の接続端子間に自動
開閉弁72を備えたバイパス管70で短絡してな
る陰圧型人工透析装置であつて、希釈用水供給系
24に設けた加熱手段36の入口側に、前記バイ
パス管70を介して透析液を流過せしめ、前記陰
圧ポンプ58より吐出される排液を分岐するため
の循環パイプ74を分岐すると共に、排液系62
ならびに該循環パイプ74のそれぞれに自動開閉
弁60,76を設け、洗滌時および消毒時には透
析液原液および希釈用水の比例ポンプ18,32
を停止し、自動開閉弁54を閉塞し、同時に自動
開閉弁60を閉塞、自動開閉弁76を開放するこ
とによつて、密閉回路90を形成せしめ、該密閉
回路90内に加熱水を循環させることができるよ
う構成することにより、従来装置に比べ自動開閉
弁の操作のみで密閉回路を形成せしめ、加熱装置
の共用により装置の簡略化が図れるばかりでなく
洗滌および消毒操作への切換えも簡便であり、装
置全体を低コストに製作することができる。
As is clear from the embodiments described above, according to the device of the present invention, a dialysate of a predetermined concentration is obtained by mixing a dialysate stock solution and dilution water preheated to an appropriate temperature by the heating means 36, and this dialysate is The dialysate passes through the negative pressure pump 42 for deaeration installed in front of the dialyzer 10, and then the dialysate is pumped to the negative pressure pump 58 installed at the outlet side of the dialyzer 10.
The dialyzer 10 via the dialysate supply system 88 under the action of
A negative-pressure artificial dialysis device configured to supply a dialysate, and further short-circuited by a bypass pipe 70 equipped with an automatic opening/closing valve 72 between connection terminals of a dialyzer 10 connected to the dialysate supply system 88, A circulation pipe 74 is provided on the inlet side of the heating means 36 provided in the dilution water supply system 24 for allowing the dialysate to flow through the bypass pipe 70 and for branching the waste fluid discharged from the negative pressure pump 58. In addition to branching, the drainage system 62
Automatic opening/closing valves 60 and 76 are provided in each of the circulation pipes 74, and proportional pumps 18 and 32 for dialysate stock solution and dilution water are provided during cleaning and disinfection.
By stopping the automatic on-off valve 54 and closing the automatic on-off valve 60 and opening the automatic on-off valve 76, a closed circuit 90 is formed, and heated water is circulated within the closed circuit 90. By configuring the system so that it can do this, compared to conventional equipment, a sealed circuit can be formed only by operating the automatic on-off valve, and the equipment can be simplified by sharing the heating device, and it is also easier to switch to cleaning and disinfection operations. Therefore, the entire device can be manufactured at low cost.

また、本考案の透析装置においては、希釈用水
供給系24に設けた給水ポンプ78の吸込み側お
よび吐出側に自動開閉弁84を備えたバイパス管
82を接続すると共に、このバイパス管82また
は自動開閉弁84の接続部より下流の希釈用水供
給系24にそれぞれチエツク弁80を接続するこ
とにより、洗滌操作時において蒸発消失された加
熱水適宜必要量を自動供給させることができ、し
かもこの場合、循環加熱水を利用した熱交換器を
介して補給し得るので、水の節約並びに熱経済的
に優れ、省エネ化を図ることができる。
In addition, in the dialysis apparatus of the present invention, a bypass pipe 82 equipped with an automatic opening/closing valve 84 is connected to the suction side and the discharge side of the water supply pump 78 provided in the dilution water supply system 24, and By connecting the check valves 80 to the dilution water supply system 24 downstream from the connection part of the valve 84, it is possible to automatically supply the required amount of heated water that has been evaporated during the cleaning operation, and in this case, the circulation Since it can be replenished via a heat exchanger that uses heated water, it is possible to save water and achieve excellent thermoeconomics, resulting in energy savings.

以上、本考案の好適な実施例について説明した
が本考案の精神を逸脱しない範囲内において種々
の改良変更をなし得ることは勿論である。
Although the preferred embodiments of the present invention have been described above, it goes without saying that various improvements and changes can be made without departing from the spirit of the present invention.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案に係る陰圧型人工透析装置の一
実施例を示す系統図、第2図は第1図に示す希釈
用水供給系に接続される比例ポンプの別の構成例
を示す系統図、第3図はさらに別の比例ポンプの
構成例を示す系統図である。 10……透析器、12……透析液タンク、14
……ポンプ、16……瀘過器、18,32……比
例ポンプ、20……原液供給系、22……逆止
弁、24……希釈用水供給系、26……自動弁、
28……減圧弁、30……圧力計、34……熱交
換器、36……ヒータ、38……弁、40……脱
気室、42……陰圧ポンプ、44……ガス抜き装
置、46……濃度計、48……安全弁、50……
弁、52……流量計、54……自動弁、56……
圧力計、58……陰圧ポンプ、60……自動開閉
弁、62……排水系、64……自動調圧弁、66
……循環パイプ、68……温度計、70……バイ
パス管、72……自動開閉弁、74……循環パイ
プ、76……自動開閉弁、78……給水ポンプ、
80……チエツク弁、82……バイパス管、84
……自動開閉弁、86……三方切換弁、88……
透析液供給系、90……密閉回路。
Fig. 1 is a system diagram showing one embodiment of the negative pressure artificial dialysis device according to the present invention, and Fig. 2 is a system diagram showing another example of the configuration of the proportional pump connected to the dilution water supply system shown in Fig. 1. , FIG. 3 is a system diagram showing yet another example of the configuration of a proportional pump. 10... Dialyzer, 12... Dialysate tank, 14
... pump, 16 ... filter, 18, 32 ... proportional pump, 20 ... stock solution supply system, 22 ... check valve, 24 ... dilution water supply system, 26 ... automatic valve,
28... Pressure reducing valve, 30... Pressure gauge, 34... Heat exchanger, 36... Heater, 38... Valve, 40... Degassing chamber, 42... Negative pressure pump, 44... Gas venting device, 46... Concentration meter, 48... Safety valve, 50...
Valve, 52...Flowmeter, 54...Automatic valve, 56...
Pressure gauge, 58...Negative pressure pump, 60...Automatic opening/closing valve, 62...Drainage system, 64...Automatic pressure regulating valve, 66
... Circulation pipe, 68 ... Thermometer, 70 ... Bypass pipe, 72 ... Automatic on-off valve, 74 ... Circulation pipe, 76 ... Automatic on-off valve, 78 ... Water pump,
80...Check valve, 82...Bypass pipe, 84
...Automatic on-off valve, 86...Three-way switching valve, 88...
Dialysate supply system, 90... sealed circuit.

Claims (1)

【実用新案登録請求の範囲】 (1) 透析液原液と予め加熱手段36により適温に
加熱した希釈用水とを混合して所定濃度の透析
液を得、この透析液を透析器10の前に設置し
た脱気用の陰圧ポンプ42を経て、透析液10
の出口側に設けた陰圧ポンプ58の作用下に透
析液供給系88を介して透析器10に供給する
よう構成し、さらに前記透析液供給系88に接
続される透析器10の接続端子間に自動開閉弁
72を備えたバイパス管70で短絡してなる陰
圧型人工透析装置であつて、希釈用水供給系2
4に設けた加熱手段36の入口側に、前記バイ
パス管70を介して透析液を流過せしめ、前記
陰圧ポンプ58より吐出される排液を分岐する
ための循環パイプ74を分岐すると共に、排液
系62ならびに該循環パイプ74のそれぞれに
自動開閉弁60,76を設け、洗滌時および消
毒時には透析液原液および希釈用水の比例ポン
プ18,32を停止し、自動開閉弁54を閉塞
し、同時に自動開閉弁60を閉塞、自動開閉弁
76を開放することによつて、密閉回路90を
形成せしめ、該密閉回路90内に加熱水を循環
させることができるよう構成してなる陰圧型人
工透析装置。 (2) 前記希釈用水供給系24には、前記比例ポン
プ32に代え、希釈用水供給系24に給水ポン
プ78とチエツク弁80とを直列接続し、前記
給水ポンプ78の吸込側と、給水ポンプ78の
吐出側と前記チエツク弁80との間に自動開閉
弁84を備えるバイパス管を接続してなる実用
新案登録請求の範囲第1項記載の陰圧型人工透
析装置。 (3) 前記希釈用水供給系24には、前記比例ポン
プ32に代え、希釈用水供給系24に給水ポン
プ78を設け、この給水ポンプ78の吸込側と
吐出側との間に自動開閉弁84とチエツク弁8
0とを直列接続したバイパス管を接続してなる
実用新案登録請求の範囲第1項記載の陰圧型人
工透析装置。
[Scope of Claim for Utility Model Registration] (1) A dialysate solution of a predetermined concentration is obtained by mixing the dialysate stock solution and dilution water that has been heated to an appropriate temperature by the heating means 36, and this dialysate is installed in front of the dialyzer 10. The dialysate 10 passes through a negative pressure pump 42 for degassing.
The dialyzer 10 is configured to be supplied to the dialyzer 10 via a dialysate supply system 88 under the action of a negative pressure pump 58 provided on the outlet side of the This is a negative pressure type artificial dialysis device in which the dilution water supply system 2 is short-circuited with a bypass pipe 70 equipped with an automatic opening/closing valve 72.
At the inlet side of the heating means 36 provided at 4, a circulation pipe 74 is branched to allow the dialysate to flow through the bypass pipe 70 and to branch the waste fluid discharged from the negative pressure pump 58. Automatic opening/closing valves 60, 76 are provided in each of the drainage system 62 and the circulation pipe 74, and during cleaning and disinfection, the proportional pumps 18, 32 of dialysate stock solution and dilution water are stopped, and the automatic opening/closing valve 54 is closed. At the same time, the automatic opening/closing valve 60 is closed and the automatic opening/closing valve 76 is opened to form a closed circuit 90, and heated water can be circulated within the closed circuit 90. Negative pressure artificial dialysis Device. (2) In the dilution water supply system 24, instead of the proportional pump 32, a water supply pump 78 and a check valve 80 are connected in series to the dilution water supply system 24, and the suction side of the water supply pump 78 and the water supply pump 78 are connected in series. The negative pressure type artificial dialysis apparatus according to claim 1, which is a registered utility model, wherein a bypass pipe having an automatic opening/closing valve 84 is connected between the discharge side of the dialysis machine and the check valve 80. (3) The dilution water supply system 24 is provided with a water supply pump 78 instead of the proportional pump 32, and an automatic on-off valve 84 is provided between the suction side and the discharge side of the water supply pump 78. Check valve 8
1. A negative pressure artificial dialysis apparatus according to claim 1, which is connected to a bypass pipe connected in series with 0 and 0.
JP3984786U 1986-03-20 1986-03-20 Expired JPH019573Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3984786U JPH019573Y2 (en) 1986-03-20 1986-03-20

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3984786U JPH019573Y2 (en) 1986-03-20 1986-03-20

Publications (2)

Publication Number Publication Date
JPS61163654U JPS61163654U (en) 1986-10-09
JPH019573Y2 true JPH019573Y2 (en) 1989-03-16

Family

ID=30548179

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3984786U Expired JPH019573Y2 (en) 1986-03-20 1986-03-20

Country Status (1)

Country Link
JP (1) JPH019573Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5973126B2 (en) * 2010-11-09 2016-08-23 ニプロ株式会社 Hot water drainage system in the dialysis machine used for hot water disinfection

Also Published As

Publication number Publication date
JPS61163654U (en) 1986-10-09

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