JPH0549869A - Concentration adjusting device of dialyzable liquid - Google Patents
Concentration adjusting device of dialyzable liquidInfo
- Publication number
- JPH0549869A JPH0549869A JP3200192A JP20019291A JPH0549869A JP H0549869 A JPH0549869 A JP H0549869A JP 3200192 A JP3200192 A JP 3200192A JP 20019291 A JP20019291 A JP 20019291A JP H0549869 A JPH0549869 A JP H0549869A
- Authority
- JP
- Japan
- Prior art keywords
- concentration
- dialysate
- stock solution
- flow rate
- liquid
- 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
Links
- 239000007788 liquid Substances 0.000 title abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 239000000126 substance Substances 0.000 claims abstract description 9
- 239000011550 stock solution Substances 0.000 claims description 64
- 238000002347 injection Methods 0.000 claims description 41
- 239000007924 injection Substances 0.000 claims description 41
- 239000000243 solution Substances 0.000 claims description 19
- 238000007865 diluting Methods 0.000 claims description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 12
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 10
- 238000000502 dialysis Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 235000014666 liquid concentrate Nutrition 0.000 description 5
- 235000017557 sodium bicarbonate Nutrition 0.000 description 5
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000013459 approach Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 235000008504 concentrate Nutrition 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000001631 haemodialysis Methods 0.000 description 2
- 230000000322 hemodialysis Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
Landscapes
- External Artificial Organs (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、個人用透析装置または
多人数用透析液供給装置における透析液の濃度調整装置
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dialysate concentration adjusting device for a personal dialysis device or a dialysate supply device for a large number of people.
【0002】[0002]
【従来の技術】人工透析を行うにあたって、血液透析装
置の透析液を目標濃度に安定して濃度調整することは、
治療的見地からみて処方上有効かつ重要であり、迅速に
目標濃度に達することは、経済的で効率よく透析を実施
するのに適している。最近では、透析液原液として透析
液の主成分である塩化ナトリウム、塩化カリウム、酢酸
ナトリウムなどからなる濃縮水溶液(以下、A原液とい
う)と、透析液の一成分である炭酸水素ナトリウムの濃
縮水溶液(以下、B原液という)の2液を準備し、使用
直前に上記2液と水とを希釈混合したバイカーボネート
透析液を用いる透析が一般的に行われるようになってき
た。2. Description of the Related Art In performing artificial dialysis, it is necessary to stably adjust the concentration of a dialysate in a hemodialysis machine to a target concentration.
From a therapeutic point of view, it is effective and important in terms of prescription, and reaching the target concentration quickly is suitable for performing dialysis economically and efficiently. Recently, a concentrated aqueous solution containing sodium chloride, potassium chloride, sodium acetate, etc., which are the main components of the dialysate (hereinafter referred to as "A stock solution"), and a concentrated aqueous solution of sodium hydrogencarbonate as one component of the dialysate ( Hereinafter, dialysis using a bicarbonate dialysate prepared by diluting and mixing the above two solutions with water has been generally performed by preparing two solutions (hereinafter, referred to as B stock solution).
【0003】[0003]
【発明が解決しようとする課題】透析液原液と炭酸水素
ナトリウムの濃縮原液が、常に一定の濃度が保証されて
供給される場合には、透析液を得るためにこれら2種類
の原液と水をその処方通りに、所定の体積比で混合希釈
すればよい。しかし、炭酸水素ナトリウムは粉末の状態
で供給されることが多く、使用前に水に溶かして水溶液
とし濃縮原液としなければならない。このように炭酸水
素ナトリウムが粉末の状態で供給される場合には、 炭酸水素ナトリウムの濃縮原液を常に正確な濃度の
水溶液とすることは困難である。従って、透析液を調整
するときに給液ポンプおよび透析液原液注入ポンプに計
量ポンプを用いて相互の送液流量を連動させて体積比が
一定になるように混合する方式では、透析液原液の濃度
が正確に規定濃度に希釈されていない場合には、図4に
示すごとく目標濃度に達せず、誤差を有したまま一定の
濃度となる(なお、図4は濃度調整の開始時からの透析
液の濃度を示す図であり、図において横軸は時間を示
し、縦軸は透析液の濃度を示している)。When the dialysate stock solution and the concentrated stock solution of sodium hydrogencarbonate are always supplied with a guaranteed constant concentration, these two stock solutions and water are used to obtain the dialysate. It may be mixed and diluted in a predetermined volume ratio according to the prescription. However, sodium hydrogen carbonate is often supplied in the form of powder, and must be dissolved in water to form an aqueous solution and a concentrated stock solution before use. Thus, when sodium hydrogen carbonate is supplied in the form of powder, it is difficult to always prepare a concentrated stock solution of sodium hydrogen carbonate as an aqueous solution having an accurate concentration. Therefore, when the dialysate is adjusted so that the volume ratio becomes constant by interlocking the feed flow rates of the dialysate pump and the dialysate stock injection pump with the metering pumps, the mixing rate of the dialysate stock solution is adjusted. If the concentration is not exactly diluted to the specified concentration, the target concentration will not be reached as shown in FIG. 4, and the concentration will remain constant with an error (FIG. 4 shows dialysis from the start of concentration adjustment). It is a figure which shows the density | concentration of a liquid, a horizontal axis shows time in the figure, and the vertical axis | shaft has shown the density | concentration of a dialysate.).
【0004】 濃度センサーを用いて、必要な濃度に
なるように比例制御、微分制御、積分制御またはそれら
の複合型の制御を行って透析液原液注入ポンプの送液流
量を変化させて透析液を調整する方式では、希釈液が混
合槽で均一になるまでに相当の時間を要するので、希釈
時の透析液原液注入ポンプの送液流量と、その時点の濃
度を濃度センサーで検知するまでの間に時間差が発生す
る。そのために、制御定数の決定が困難であり、最適な
制御が難しく、図5に示すごとく目標濃度に安定するま
でに相当の時間がかかる。などの欠点が顕著であった。A concentration sensor is used to perform proportional control, derivative control, integral control, or a composite type control thereof so that a required concentration is achieved, and the dialysate is supplied by changing the flow rate of the dialysate concentrate injection pump. In the adjustment method, it takes a considerable amount of time for the diluted solution to become uniform in the mixing tank.Therefore, the flow rate of the dialysate stock solution injection pump at the time of dilution and the time until the concentration sensor detects the concentration Time difference occurs. Therefore, it is difficult to determine the control constant, and it is difficult to perform optimum control, and it takes a considerable time to stabilize the target concentration as shown in FIG. Defects such as were remarkable.
【0005】従って、従来の装置では精度良く濃度を調
整できなかったり、または精度良く濃度を調整できたと
しても時間がかかり、その間大量の透析液が無駄になっ
ていた。本発明は、上記課題を解決して、透析液濃度を
迅速に目標濃度到達させ、その濃度を安定に維持させる
透析液の濃度調整装置を提供することを課題とするもの
である。Therefore, in the conventional apparatus, the concentration cannot be adjusted accurately, or even if the concentration can be adjusted accurately, it takes time, and a large amount of dialysate is wasted during that time. An object of the present invention is to solve the above-mentioned problems and to provide a dialysate concentration adjusting device that allows a dialysate concentration to reach a target concentration quickly and maintains the concentration stably.
【0006】[0006]
【課題を解決するための手段】本発明は、給水ライン
と、透析液原液供給ラインと、前記透析液原液供給ライ
ンから供給される透析液原液を所定の流量で送液する透
析液原液注入ポンプと、前記給水ラインから供給される
水によって前記透析液原液注入ポンプから供給される透
析液原液を希釈混合するための混合槽と、前記混合され
た薬液の濃度を測定する濃度センサーと、前記透析液原
液と水とで調合された透析液を透析器に供給する給液ポ
ンプと、前記濃度センサーからの信号を受けて前記透析
液原液注入ポンプの送液流量を制御するための制御部と
からなる透析液の濃度調整装置であって、濃度が予め定
めた所定の濃度範囲外にあるときは、前記濃度センサー
で測定した濃度が前記予め定めた所定の濃度範囲内に達
するまで若しくはさらにその後所定の期間、前記透析液
原液注入ポンプの送液流量を予め定めた所定の流量で濃
度を調節して、濃度が前記予め定めた所定の範囲内にあ
るときは前記濃度センサーにより測定した濃度によって
前記透析液原液注入ポンプの送液流量を変化させて濃度
を調節することを特徴とするものである。The present invention is directed to a water supply line, a dialysate stock solution supply line, and a dialysate stock solution injection pump for delivering the dialysate stock solution supplied from the dialysate stock solution supply line at a predetermined flow rate. A mixing tank for diluting and mixing the dialysate stock solution supplied from the dialysate stock solution injection pump with water supplied from the water supply line; a concentration sensor for measuring the concentration of the mixed chemical solution; From a liquid supply pump that supplies a dialysate prepared by a liquid concentrate and water to a dialyzer, and a control unit that receives a signal from the concentration sensor and controls the flow rate of the dialysate concentrate injection pump. When the concentration is outside the predetermined concentration range determined in advance, the concentration measured by the concentration sensor reaches the predetermined concentration range determined in advance or Then, for a predetermined period of time, the concentration of the dialysate stock solution injection pump was adjusted at a predetermined flow rate, and when the concentration was within the predetermined range, it was measured by the concentration sensor. It is characterized in that the flow rate of the dialysate stock solution injection pump is changed according to the concentration to adjust the concentration.
【0007】更に本発明においては、濃度が前記予め定
めた所定の範囲内にあるときは、透析液原液注入ポンプ
の送液流量を変化させて調整するが、所定の期間が経過
するまでその送液流量を維持するか、もしくは濃度が予
め定めた目標濃度との許容誤差内に入るまで調整する。
そして、薬液濃度センサーによる濃度の測定を繰り返
し、透析液の濃度が上記予め定めた目標濃度との許容誤
差内に入るようにしている。Further, in the present invention, when the concentration is within the above-mentioned predetermined range, the flow rate of the dialysate stock solution injection pump is adjusted by changing it. The liquid flow rate is maintained or the concentration is adjusted until it is within an allowable error with a predetermined target concentration.
Then, the concentration measurement by the chemical concentration sensor is repeated so that the concentration of the dialysate falls within an allowable error with respect to the predetermined target concentration.
【0008】前記透析液原液注入ポンプの送液流量変更
の計算には、比例制御、微分制御、積分制御またはこれ
らの複合型による演算、その他マイクロコンピューター
によりさまざまな制御を用いることができる。目標濃度
との差が大きいときには、段階的に目標濃度に近づくよ
うに変化幅の最大値を規制するなどの演算処理を行うこ
とが可能である。また、前記透析液原液注入ポンプの初
期流量の値として、目標値に安定に濃度調整されている
ときの送液流量を用いるのがよい。In the calculation of the change in the delivery flow rate of the dialysate stock solution injecting pump, various controls by proportional control, derivative control, integral control or a combination of these, and other microcomputers can be used. When the difference from the target density is large, it is possible to perform arithmetic processing such as restricting the maximum value of the change width so as to gradually approach the target density. Further, as the value of the initial flow rate of the dialysate undiluted solution injection pump, it is preferable to use the solution delivery flow rate when the concentration is stably adjusted to the target value.
【0009】[0009]
【作用】透析液の濃度調整は以下の順序で行われる。す
なわち、 ステップ1: 濃度調整を開始したときは、透析液原液
注入ポンプの送液流量をあらかじめ定めた一定の初期流
量で運転を開始する。 ステップ2: 濃度が予め定めた所定の濃度範囲外にあ
るときは、薬液濃度センサーで測定した濃度が濃度範囲
内に達するまで、若しくはさらにその後の所定期間、透
析液原液注入ポンプの送液流量を初期流量で運転して、
迅速に目標濃度に近づけ、濃度が予め定めた所定の濃度
範囲内に達するようにし、上記期間が過ぎた後、ステッ
プ3に進む。[Function] The concentration of the dialysate is adjusted in the following order. That is, Step 1: When the concentration adjustment is started, the dialysate stock solution injection pump is started at a constant initial flow rate. Step 2: When the concentration is out of the predetermined concentration range determined in advance, the flow rate of the dialysate undiluted solution injection pump is adjusted until the concentration measured by the chemical concentration sensor reaches the concentration range or further for a predetermined period thereafter. Run at the initial flow rate,
The concentration is quickly brought close to the target concentration so that the concentration reaches a predetermined concentration range, and after the above period has passed, the process proceeds to step 3.
【0010】ステップ3: 濃度が上記範囲内にあると
きは、薬液濃度センサーにより測定した実際の濃度によ
って透析液原液注入ポンプの送液流量を変化させ、その
送液流量を所定の期間維持して目標濃度に近づける。或
は濃度が予め定めた目標濃度との許容誤差を越えるまで
濃度の調整を行い、その後ステップ3を繰り返す。濃度
が前記濃度範囲外になったときは、ステップ2に移行す
る。という調整をおこなう。Step 3: When the concentration is within the above range, the flow rate of the dialysate stock solution injection pump is changed according to the actual concentration measured by the chemical concentration sensor, and the flow rate is maintained for a predetermined period. Bring it closer to the target concentration. Alternatively, the density is adjusted until the density exceeds an allowable error with respect to a predetermined target density, and then step 3 is repeated. When the density is out of the density range, the process proceeds to step 2. Adjustment.
【0011】濃度が予め定めた所定の濃度範囲外にある
ときは、透析液原液注入ポンプの送液流量を予め定めた
所定の流量で運転し、薬液濃度センサーで測定した濃度
が濃度範囲内に達するまで、もしくはさらにその後の所
定期間、前記透析液原液注入ポンプの送液流量を前記初
期流量で調整するので濃度を迅速に目標濃度に近づける
ことができる。When the concentration is out of the predetermined concentration range, the dialysate stock solution injection pump is operated at a predetermined flow rate so that the concentration measured by the chemical concentration sensor is within the concentration range. The concentration of the dialysate solution injection pump is adjusted by the initial flow rate until it reaches the target value or further for a predetermined period thereafter, so that the concentration can be quickly brought close to the target concentration.
【0012】また、濃度が上記予め定めた所定の濃度範
囲にあるときは、薬液濃度センサーにより測定した実際
の濃度を用いて目標濃度に近づくように前記透析液原液
注入ポンプの送液流量を変化させて、その送液流量を維
持したまま、ある一定期間経過が経過するまで、もしく
は濃度が予め定めた目標濃度との許容誤差を越えるまで
調整するので精度良く透析液をその安定した濃度に維持
させることができる。When the concentration is within the above-mentioned predetermined concentration range, the flow rate of the dialysate stock solution injection pump is changed so as to approach the target concentration by using the actual concentration measured by the chemical concentration sensor. The dialysate is maintained at its stable concentration with high accuracy because the flow rate is maintained and adjusted until a certain period of time elapses or until the concentration exceeds a predetermined target tolerance error. Can be made
【0013】また、透析液の濃度のみならず、浸透圧、
電導度または成分比の調整を行うに場合にも上記のよう
な構成で調整を行うことが出来る。In addition to the concentration of dialysate, the osmotic pressure,
In the case of adjusting the electric conductivity or the component ratio, the adjustment can be performed with the above configuration.
【0014】[0014]
【実施例】以下、本発明を図面に基づいて詳細に説明す
る。図1は本発明の透析液の濃度調整装置を用いた個人
用透析装置の概略系統図であり、図において、20が本
発明の透析液の濃度調整装置である。本実施例の濃度調
整装置20は、A原液とB原液の2液を水と希釈混合し
て、バイカーボネート透析液を調整する場合を示してい
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the drawings. FIG. 1 is a schematic system diagram of a personal dialysis apparatus using the dialysate concentration adjusting apparatus of the present invention. In the figure, 20 is the dialysate concentration adjusting apparatus of the present invention. The concentration adjusting device 20 of the present embodiment shows a case where two carbonate solutions, A stock solution and B stock solution, are diluted and mixed with water to prepare a bicarbonate dialysate.
【0015】図1において 1は給水ライン、2はB原
液供給ライン、3はA原液供給ライン、4はB原液注入
ポンプ、5はA原液注入ポンプ、6はB液混合槽、7は
A液混合槽、8及び9は濃度センサー、10は給液ポン
プ、11は給液ライン、12は透析器、13はバイパス
コネクタ、14は排液ポンプ、15は排液ライン、16
は制御部である。In FIG. 1, 1 is a water supply line, 2 is a B stock solution supply line, 3 is an A stock solution supply line, 4 is a B stock solution injection pump, 5 is an A stock solution injection pump, 6 is a B solution mixing tank, and 7 is a solution A. Mixing tanks, 8 and 9 are concentration sensors, 10 is a liquid supply pump, 11 is a liquid supply line, 12 is a dialyzer, 13 is a bypass connector, 14 is a drainage pump, 15 is a drainage line, 16
Is a control unit.
【0016】透析液は、まずバイパスコネクタ13によ
り透析液の流路を形成し、A原液注入ポンプ5、B原液
注入ポンプ4、給液ポンプ10、排液ポンプ14を運転
する。この際、B液混合槽6にてB原液供給ライン2か
ら供給されるB原液を給水ライン1から供給される水に
よって希釈混合してB液希釈液を調合し、さらにA液混
合槽7にてA原液供給ライン3から供給されるA原液を
上記のB液希釈液で希釈混合してバイカーボネート透析
液が調合される。調合されたバイカーボネート透析液は
給液ポンプ10と排液ポンプ14によりバイパスコネク
タ13を介して排液ライン15を通って排出される。The dialysate first forms a dialysate flow path by the bypass connector 13 and operates the A stock solution injection pump 5, the B stock solution injection pump 4, the feed pump 10, and the drainage pump 14. At this time, the B stock solution supplied from the B stock solution supply line 2 in the B solution mixing tank 6 is diluted and mixed with the water supplied from the water supply line 1 to prepare a B solution diluent, and then the A solution mixing tank 7 is further prepared. Then, the A stock solution supplied from the A stock solution supply line 3 is diluted and mixed with the B solution diluting solution to prepare a bicarbonate dialysate. The prepared bicarbonate dialysate is discharged by the feed pump 10 and the drainage pump 14 through the drain connector 15 via the bypass connector 13.
【0017】バイカーボネート透析液の濃度調整は、給
液ポンプ10の流量とA原液注入ポンプ5の流量とB原
液注入ポンプ4の流量によって調整される。すなわち、
A原液及びB原液の量はそれぞれA原液注入ポンプ5の
流量とB原液注入ポンプ4の流量によって決定され、水
の量は給液ポンプ10の流量からA原液注入ポンプ5の
流量とB原液注入ポンプ4の流量を差し引いた量とな
る。従って、給液ポンプ10の流量とA原液注入ポンプ
5の流量とB原液注入ポンプ4の流量を制御することに
よりバイカーボネート透析液の濃度を調整することがで
きる。一般には、給液ポンプ10の流量は患者の処方に
合わせて一定に制御されるため、バイカーボネート透析
液の濃度はA原液注入ポンプ5の流量とB原液注入ポン
プ4の流量によって調整される。The concentration of the bicarbonate dialysate is adjusted by the flow rate of the feed pump 10, the A stock solution injection pump 5 and the B stock solution injection pump 4. That is,
The amounts of A stock solution and B stock solution are determined by the flow rate of the A stock solution injection pump 5 and the flow rate of the B stock solution injection pump 4, respectively, and the amount of water from the flow rate of the liquid supply pump 10 to the flow rate of the A stock solution injection pump 5 and the B stock solution injection. It is the amount obtained by subtracting the flow rate of the pump 4. Therefore, the concentration of the bicarbonate dialysate can be adjusted by controlling the flow rates of the feed liquid pump 10, the A stock solution injection pump 5, and the B stock solution injection pump 4. Generally, since the flow rate of the liquid supply pump 10 is controlled to be constant according to the patient's prescription, the concentration of the bicarbonate dialysate is adjusted by the flow rates of the A stock solution injection pump 5 and the B stock solution injection pump 4.
【0018】図2は本発明を適用した場合のバイカーボ
ネート透析液の濃度変化曲線である。図において横軸は
時間を示し、縦軸はバイカーボネート透析液の濃度を示
している。まず、濃度調整を開始した時に、例えば給液
ポンプ10を500〔ミリリットル/分〕で一定に制御
して運転し、B原液注入ポンプ4を18〔ミリリットル
/分〕、A原液注入ポンプ5を14.3〔ミリリットル
/分〕でそれぞれ一定に制御して運転する。これらの流
量は、バイカーボネート透析液の濃度が制御範囲内に入
るように予め設定しておく。制御範囲はある程度の幅を
有し、後述するフィードバック制御に適した値とするこ
とが望ましい。FIG. 2 is a concentration change curve of the bicarbonate dialysate when the present invention is applied. In the figure, the horizontal axis represents time and the vertical axis represents the concentration of the bicarbonate dialysate. First, when the concentration adjustment is started, for example, the liquid supply pump 10 is operated while being constantly controlled at 500 [ml / min], the B stock solution injection pump 4 is 18 [milliliter / minute], and the A stock solution injection pump 5 is 14 Operate with constant control of 3 [ml / min]. These flow rates are set in advance so that the concentration of the bicarbonate dialysate falls within the control range. The control range has a certain width and is preferably set to a value suitable for feedback control described later.
【0019】こうして濃度は、図2のAのように濃度が
上昇してゆき、約1分後にB点の制御範囲下限を通過し
て制御範囲内に入る。このとき、B原液は正確な処方通
りの濃度に調整されていない場合には目標濃度からずれ
たCの状態で安定する。B点を通過した時点で時間計測
を開始して、例えば2分後に濃度センサー8で濃度を測
定して、制御部16の指示により、透析液が目標濃度に
近づくようにフィードバック制御し、目標濃度との差の
分だけB原液注入ポンプ4の送液流量を増加させる。フ
ィードバック制御は、本実施例のように制御範囲内に達
した後に所定の期間おいて開始してもよいし、また制御
範囲内に達した後に直ちに開始してもよい。In this way, the concentration rises as shown by A in FIG. 2, and after about 1 minute, passes through the lower limit of the control range at point B and enters the control range. At this time, the stock solution B is stabilized in the state of C deviating from the target concentration unless the concentration is exactly adjusted according to the prescription. Time measurement is started at the time when the point B is passed, the concentration is measured by the concentration sensor 8 after, for example, 2 minutes, and feedback control is performed according to an instruction from the control unit 16 so that the dialysate approaches the target concentration. The feed rate of the B stock solution injection pump 4 is increased by the amount of the difference between and. The feedback control may be started within a predetermined period after reaching the control range as in the present embodiment, or may be started immediately after reaching the control range.
【0020】このようにして透析液の濃度はDのごとく
濃度調整開始後約3分で容易に目標濃度に到達すること
ができる。以後2分毎にこの操作を繰り返してゆけば、
目標濃度に安定したバイカーボネート透析液を得ること
ができる。また、図3は濃度が安定しているときに、目
標濃度からの誤差が発生したときの濃度変化曲線であ
る。上記のように、2分毎に濃度の補正操作を行ってい
るので、例えばE点に示すような外乱による目標濃度か
らの誤差が発生したとき、F点に示すように2分以内に
その誤差を検知して、B原液注入ポンプ4の送液流量を
変化させ、一定時間、この場合2分間維持することによ
り濃度を目標濃度との許容誤差内に入れることが出来
る。この場合、約1分でG点に示すように、目標濃度に
復帰する事が出来る。In this way, the concentration of the dialysate can easily reach the target concentration about 3 minutes after the start of concentration adjustment as shown by D. After that, if you repeat this operation every 2 minutes,
A bicarbonate dialysate stable to the target concentration can be obtained. Further, FIG. 3 is a density change curve when an error from the target density occurs when the density is stable. As described above, since the density correction operation is performed every 2 minutes, when an error from the target density due to a disturbance such as that shown at point E occurs, the error is corrected within 2 minutes as shown at point F. Is detected and the flow rate of the solution to be pumped by the B stock solution injection pump 4 is changed and maintained for a fixed time, in this case, 2 minutes, so that the concentration can be brought within an allowable error from the target concentration. In this case, it is possible to return to the target density as shown at the point G in about 1 minute.
【0021】透析液A原液に対しても同様に濃度センサ
ー9で濃度を測定して、制御部16の指示により、A原
液注入ポンプの流量を変化させると、濃度調整開始後約
3分で、目標濃度に安定したバイカーボネート透析液を
調整することができる。以上のように速やかに透析液を
調合することができ、バイパスコネクタ13を解放し、
透析器12に正確に調合された透析液を供給することが
できる。また、透析液の濃度が変化した場合にも、速や
かに濃度を修正することが可能である。Similarly, the concentration of the dialysate A stock solution is measured by the concentration sensor 9, and when the flow rate of the stock solution injection pump A is changed according to the instruction of the control unit 16, about 3 minutes after the start of the concentration adjustment, A stable bicarbonate dialysate can be adjusted to a target concentration. As described above, the dialysate can be rapidly prepared, the bypass connector 13 is released,
It is possible to supply the dialyser 12 with an accurately prepared dialysate. Further, even if the concentration of the dialysate changes, the concentration can be corrected promptly.
【0022】[0022]
【発明の効果】薬液の希釈混合に、本発明の濃度調整装
置を用いると、迅速に濃度を安定させることができるの
で、原液の無駄な消費量が少なくなり、さらに装置使用
前の準備運転時間が短縮されるので、経済的な効果が上
げられるうえに、作業の待ち時間が短縮されるので、効
率的な装置の稼働を実現させることができる。また、薬
液濃度を目標濃度に安定させることができるために、処
方上の適正濃度の調整に有効である。When the concentration adjusting device of the present invention is used for diluting and mixing chemicals, the concentration can be stabilized quickly, so that the wasteful consumption of the stock solution is reduced, and the preparation operation time before using the device is reduced. Since the time is shortened, the economical effect is improved, and the waiting time for the work is shortened, so that the efficient operation of the device can be realized. Further, since the concentration of the drug solution can be stabilized at the target concentration, it is effective for adjusting the proper concentration in prescription.
【図1】本発明の濃度調整装置を用いた血液透析装置の
概略系統図である。FIG. 1 is a schematic system diagram of a hemodialysis apparatus using a concentration adjusting device of the present invention.
【図2】本発明の濃度調整装置による濃度調整開始時の
濃度変化曲線を示す図である。FIG. 2 is a diagram showing a density change curve at the start of density adjustment by the density adjusting apparatus of the present invention.
【図3】本発明の濃度調整装置による濃度安定時の濃度
変化曲線を示す図である。FIG. 3 is a diagram showing a concentration change curve when the concentration is stabilized by the concentration adjusting device of the present invention.
【図4】従来の濃度調整装置による濃度調整開始時の濃
度変化曲線を示す図である。FIG. 4 is a diagram showing a density change curve at the start of density adjustment by a conventional density adjusting device.
【図5】従来の濃度調整装置による濃度調整開始時の濃
度変化曲線を示す図である。FIG. 5 is a diagram showing a density change curve at the start of density adjustment by a conventional density adjusting device.
1 給液ライン 2 B原液供給ライン 3 A原液供給ライン 4 B原液注入ポンプ 5 A原液注入ポンプ 6 B液混合槽 7 A液混合槽 8 濃度センサー 9 濃度センサー 10 給液ポンプ 11 給液ライン 12 透析器 13 バイパスコネクタ 14 排液ポンプ 15 排液ライン 16 制御部 20 濃度調整装置 1 Liquid supply line 2 B liquid concentrate supply line 3 A liquid concentrate supply line 4 B liquid concentrate injection pump 5 A liquid concentrate injection pump 6 Liquid B mixing tank 7 Liquid A mixing tank 8 Concentration sensor 9 Concentration sensor 10 Liquid supply pump 11 Liquid supply line 12 Dialysis Device 13 bypass connector 14 drainage pump 15 drainage line 16 control unit 20 concentration adjusting device
Claims (1)
と、前記透析液原液供給ラインから供給される透析液原
液を所定の流量で送液する透析液原液注入ポンプと、前
記給水ラインから供給される水によって前記透析液原液
注入ポンプから供給される透析液原液を希釈混合するた
めの混合槽と、前記混合された薬液の濃度を測定する濃
度センサーと、前記透析液原液と水とで調合された透析
液を透析器に供給する給液ポンプと、前記濃度センサー
からの信号を受けて前記透析液原液注入ポンプの送液流
量を制御するための制御部とからなる透析液の濃度調整
装置であって、濃度が予め定めた所定の濃度範囲外にあ
るときは、前記濃度センサーで測定した濃度が前記予め
定めた所定の濃度範囲内に達するまで若しくはさらにそ
の後所定の期間、前記透析液原液注入ポンプの送液流量
を予め定めた所定の流量で濃度を調節して、濃度が前記
予め定めた所定の範囲内にあるときは前記濃度センサー
により測定した濃度によって前記透析液原液注入ポンプ
の送液流量を変化させて濃度を調節することを特徴とす
る透析液の濃度調整装置。1. A water supply line, a dialysate stock solution supply line, a dialysate stock solution injection pump for sending a dialysate stock solution supplied from the dialysate stock solution supply line at a predetermined flow rate, and a supply line supplied from the water supply line. A mixing tank for diluting and mixing the dialysate stock solution supplied from the dialysate stock solution injection pump with water, a concentration sensor for measuring the concentration of the mixed chemical solution, and the dialysate stock solution and water. A dialysate concentration adjusting device comprising a supply pump for supplying dialysate to a dialyzer, and a control unit for receiving a signal from the concentration sensor and controlling the flow rate of the dialysate stock injection pump. Therefore, when the concentration is outside the predetermined concentration range determined in advance, until the concentration measured by the concentration sensor reaches within the predetermined concentration range determined in advance, or further for a predetermined period, The dialysate stock solution injection pump adjusts the concentration by a predetermined flow rate, and when the concentration is within the predetermined range, the dialysate stock solution is injected according to the concentration measured by the concentration sensor. A dialysate concentration adjusting device, wherein the concentration of the dialysate is adjusted by changing the flow rate of the pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3200192A JPH0549869A (en) | 1991-08-09 | 1991-08-09 | Concentration adjusting device of dialyzable liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3200192A JPH0549869A (en) | 1991-08-09 | 1991-08-09 | Concentration adjusting device of dialyzable liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0549869A true JPH0549869A (en) | 1993-03-02 |
Family
ID=16420330
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3200192A Pending JPH0549869A (en) | 1991-08-09 | 1991-08-09 | Concentration adjusting device of dialyzable liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0549869A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009279110A (en) * | 2008-05-21 | 2009-12-03 | Jms Co Ltd | Hemodialysis system |
| JP2013052229A (en) * | 2011-08-09 | 2013-03-21 | Kawasumi Lab Inc | Blood purification device and blood purification system |
| JP2014193376A (en) * | 2008-07-09 | 2014-10-09 | Baxter Internatl Inc | Dialysis system having inventory management including online dextrose mixing |
| JP2018082904A (en) * | 2016-11-24 | 2018-05-31 | 医療法人社団 誠仁会 | Dialysis system |
| JP2021035662A (en) * | 2019-08-30 | 2021-03-04 | 日機装株式会社 | Mixer |
| JP2023029841A (en) * | 2008-07-09 | 2023-03-07 | バクスター・インターナショナル・インコーポレイテッド | Dialysis method including wireless patient data |
-
1991
- 1991-08-09 JP JP3200192A patent/JPH0549869A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009279110A (en) * | 2008-05-21 | 2009-12-03 | Jms Co Ltd | Hemodialysis system |
| JP2014193376A (en) * | 2008-07-09 | 2014-10-09 | Baxter Internatl Inc | Dialysis system having inventory management including online dextrose mixing |
| JP2023029841A (en) * | 2008-07-09 | 2023-03-07 | バクスター・インターナショナル・インコーポレイテッド | Dialysis method including wireless patient data |
| JP2013052229A (en) * | 2011-08-09 | 2013-03-21 | Kawasumi Lab Inc | Blood purification device and blood purification system |
| JP2018082904A (en) * | 2016-11-24 | 2018-05-31 | 医療法人社団 誠仁会 | Dialysis system |
| JP2021035662A (en) * | 2019-08-30 | 2021-03-04 | 日機装株式会社 | Mixer |
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