WO1985001221A1 - Membrane separator - Google Patents

Membrane separator Download PDF

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Publication number
WO1985001221A1
WO1985001221A1 PCT/JP1983/000311 JP8300311W WO8501221A1 WO 1985001221 A1 WO1985001221 A1 WO 1985001221A1 JP 8300311 W JP8300311 W JP 8300311W WO 8501221 A1 WO8501221 A1 WO 8501221A1
Authority
WO
WIPO (PCT)
Prior art keywords
power
pressure
pump
semi
flow rate
Prior art date
Application number
PCT/JP1983/000311
Other languages
French (fr)
Japanese (ja)
Inventor
Koichi Yamada
Ichiro Hiraiwa
Shin Taniguchi
Toshinari Zengo
Original Assignee
Ebara Corporation
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 Ebara Corporation filed Critical Ebara Corporation
Priority to PCT/JP1983/000311 priority Critical patent/WO1985001221A1/en
Priority to FR848414385A priority patent/FR2551989B1/en
Publication of WO1985001221A1 publication Critical patent/WO1985001221A1/en

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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
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/06Energy recovery
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/24Specific pressurizing or depressurizing means
    • B01D2313/246Energy recovery means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/90Additional auxiliary systems integrated with the module or apparatus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/90Additional auxiliary systems integrated with the module or apparatus
    • B01D2313/903Integrated control or detection device

Definitions

  • the traditional c banquet of Huo Yi Zhi » is structured as shown in the No. 1 / aa flow chart.
  • the dew / B is an example of seawater in the seawater / 0, which is not shown in the drawing and is unreasonable.
  • the pump / the discharge pressure, discharge rate, discharge in the Ko ⁇ 0 beta, through 8 ⁇ ChikaraiHajikamiben a be more Seimai the pressure sensing ⁇ 2 * semipermeable membrane * Schlenk f
  • the key is returned by the activator J.
  • the energy stripped by the bin is used to assist the pump motor f.
  • the driving method was to use only the sparse cut-off rate, and to minimize the shaft power of the pump / semi-transparency * with the maximum permissible inspection car.
  • the conventional technology arrived only on a domestic vehicle with a dilute solution. Since the power recovered by «was not taken into account, the power consumed was not minimal.
  • the required power of the pump and the power ft of the pump are set to be the minimum in the garden in a large-scale separable storage device.
  • the present invention relates to a pump and a motor
  • the present invention relates to a performance curve of a pump, a performance curve of a power control means, and
  • the present invention relates to a pump for pressurized excitation of a liquid, a pump and a semi-permeable membrane interposed in the piping of the IW, a semi-permeable membrane, and a semi-permeable membrane.
  • a semi-permeable membrane the quality of the liquid in the sap is obtained using the semi-permeable membrane.
  • the liquid supply volume, liquid supply pressure, trace flow volume, test liquid pressure, volume and pressure such as C at the turning point where the minimum required power is obtained are determined.
  • OMFI L ⁇ ⁇ ⁇ ⁇ ⁇ Amago ginger can also be used.
  • the claim of the present invention is characterized in that the pump and the semi-permeable SIM piping are provided with a pressure-intensifying means or a strain-detecting means A in the claim / claim and a & box indication is calculated.
  • a wide-spreading device equipped with a pressure regulating valve opening and a power garden hand ft to adjust the opening of the power control valve so that it is equal to the pressure in the system or the system in the system It is.
  • the * claim is a semi-transparent recommendation and an energizing means in claim / claim.
  • ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ 3 ⁇ 4 3 ⁇ 4 3 ⁇ 4 This device is equipped with a control circuit that provides a power circuit or a pressure regulating valve to make it equal.
  • the seventh claim is the invention according to any one of the claims / claims to which the minimum required power is calculated.
  • the main unit is the pump, the power ⁇ , and the discharge of the pump, as shown above. Calculating the point of minimum supper power within the standard of the detention system based on the census of the clan quality and the penetration of the garden «The high pressure pump that occupies the food has the effect of making it possible to reduce C.
  • the force detecting means (or the collecting amount detecting means) was cultivated in the pipe of the 4r corrosive liquid in the pipe of the present invention, and the loss of the force was detected in the system.
  • the procedure is simple.
  • Solution / is the flow sheet for fermentation, and joy ⁇ 2 »is the line 8 that explains the pressure and the amount of lipolysis in the film as it is placed. Line showing the power of the plant and the power lost
  • FIG. 7 is a fireman's standard si showing one block of interdigital 4 a.
  • Fig. ⁇ Is a horizontal line with a line S indicating the relationship between the valve loss due to the pressure return valve and the amount of dilute solution (recharge water). Is taken.
  • Yuma A is a pump
  • curves ⁇ , ⁇ are £ force adjustment valve ⁇ surface force when squeezed? ! ! And «to be confined to the surface».
  • Curve 0 is more inclusive of the so-called pressure increase than song summary ⁇ .
  • the power L VL for the pressure loss in the circuit is the resistance of the pressure regulating valve.
  • M IL pump / is a composite of Kosatsuki ft line ⁇ the turbines 7 respectively, the power loss at the maximum efficiency point near ⁇ of ⁇
  • the feeding power I of the motor f has a large pump / discharge itE power, and the SIR vehicle is large and small.
  • the motor f has a smaller power I at the lower end of the shaft (power E), which is less power-saving.
  • the hydration power ⁇ is high in the low-low flow area and high-pressure area, and its local minimum value is located in the middle of the garden.
  • SRW is performed by the 488th block S of the present invention.
  • the Poiuxa is obtained.
  • the method shown in Fig. 10 is used to calculate the discharge amount ⁇ supplied to the membrane from the dilute liquid mm.
  • the pump performance curve A will be used to determine the pump / discharge rate ⁇ .
  • Liquid concentration G M supply salary of Toru ⁇ is ⁇ C Q of Hiroshi inlet liquid, concentrated
  • Calculate the retention ⁇ by A constant value may be used for small meals where the amount of liquid / change is small.
  • the dilute i which is degraded by the SE force ⁇ ⁇ , is a first-order specific example. 13 ⁇ 40AL0 calculated by the formula ⁇ .
  • JT is specified, and then to clause (1). (7) The loop is repeated.
  • Steps 8 to m above can be omitted by weaving them as a mathematical table.
  • the maximum bomb discharge EE power ⁇ is input to the maximum power calculator / *.
  • the S / S power ⁇ HAZi is the maximum E force determined from the properties of the semi-permeable *, calculated from the pumping curve, and the pump / Is the maximum pressure determined by the pumping plane. Therefore, the maximum E force allowed as a prosthesis is the smaller of ⁇ ⁇ ⁇ ,,? ⁇ ⁇ 2, and the maximum pressure calculation S / # compares the E force P 0KAX , and finds the smaller ⁇ I'll do it.
  • Discharge power calculation S / 4 has a pressure of a force of a maximum of £ power / * Pressure, which is the output of number generation S, is input.
  • »constant" operation 1WSI N which is set at t 7 is input, if e ⁇
  • the M number generator * 3 outputs « .as » M from the permeation £ ⁇ -f (OK)) and calculates the pressure ⁇ ⁇ Input to 2.
  • the continuous trace flow is calculated from the
  • the concentrated liquid pressure of 0 C which is the pressure of the liquid to be supplied to the bin 7 3 ⁇ 4 2 is supplied to the bin 7.
  • the turbine generation power is calculated from the continuous amount 2 input to ,? 2 ) «Calculate and output, and input to the previously described motor
  • Minimum power calculation ⁇ 7 is 1-,,, ⁇ 2 ⁇ L (i + /) Ask. Then, the motor power train L (to LI) is calculated to find the dimming ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ Be able to pass through ⁇
  • Sought is 3 ⁇ 4 beta in because they definite to JR, £ valve opening force adjusting valve than is required. An operation similar to C is performed, and the valve opening A T1 is output, and the valve mechanism is exposed by a servo mechanism that does not indicate H *.
  • the amount A of the vial inlet well J is determined from the following equation.
  • the E-force regulating valve a may be returned by the SE force lateral ffi »2» so that the force at the determination point matches the calculation.
  • the pressure of the pressure from the semi-permeable membrane * (not shown) is reduced by the minimum power L mi *.
  • the power recovery device may be driven back by the pressure generator to obtain hydraulic power.
  • a BE power detector a » is provided in the supply pipe or the power supply pipe is connected to the concentrated liquid pipe. It is also possible to displace the EE force adjusting valve or the exciting force S so as to provide a small amount of power by imaging the EE force adjusting valve or the exciting force S (not shown). Therefore, provision is made for detecting the volume of piping from the pump / to the semi-permeable *
  • a pressure regulating valve such that the% amount of the concentrated liquid detected by the fiber amount detecting means is a fiber liquid amount corresponding to the minimum power.
  • the food is sent to a table meal, which is a must-have meal, especially for the ingestion of seawater, but 1K is used for other medicines A, food and other fibers.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Nanotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A membrane separator wherein a substance is separated out by employing a semipermeable membrane to obtain either a dilute or a concentrated solution or both. The most economical operation of the membrane separator obtains a maximum amount of a desired liquid with minimum energy, that is, minimizing the amount of energy required per unit of obtained solution. Hitherto, minimum power is obtained at the maximum pressure corresponding to the performance of the semipermeable membrane; consequently, the energy required is not the minimum. According to the invention, there is provided a membrane separator comprising a flow rate controller provided with a control circuit for calculating the minimum necessary power at the flow rate of a dilute or concentrated solution, set according to the pump performance curve, the power-recovering means performance curve and the relationship between the concentration and osmotic pressure of a solute in the solution, wherein the power-recovering means performance curve is also taken into consideration. An embodiment of the invention is provided with a means for detecting the flow rate of a liquid supplied to the membrane separator or of a concentrated or dilute solution therefrom, and a control circuit for adjusting a pressure-regulating valve or a power-recovering means so that the value from the flow rate detecting means is coincident with the theoretical flow rate in the system. Alternately, the flow rate detecting means is provided with, as a pressure detecting means, a control circuit for adjusting the pressure-regulating valve or the power-recovering means so that the value indicated by the pressure detecting means is coincident with the pressure corresponding to the theoretical pressure in the system. The flow rate or pressure detecting means is disposed between a pump and a semipermeable membrane or in the part of a piping for concentrated solution which is on the downstream side of the semipermeable membrane.

Description

, 續 香 膿分讓襄置  , Continue incense
技 術 分 野  Technical field
S 本発屬は腐分讓襄置に於ける省動力運核に講するも のである。  S The origin of this genera is to focus on power-saving nuclei in the decay process.
背 景 技 術  Background technology
¾来例の cの霍義置の主餐 »は第 / aaのフ ロ ーシ 一 トに示すよう 構成されている。 露 / Bは海水澳水化 /0 の例 示すもので理示されない取水義置から取水して 翁 Λ疆された海水は高圧の遠心ポンプ (以下拳にボン ブと稀す) / に藪込まれ、 ポンプ / で吐出圧力 、 吐 出量 、 濃麼 0βに して吐出し、 圧力検出讎 <2 *に より制舞される 8Ξ力謂薑弁 aを通り、 半透膜 *の手練 f の ffiカ梭出 S J *の圧力漏定点 'をとおり、 半透厲 * の片儒に入り、 厲面 EE力 により浸透圧に抗して ¾ 量 ,の滅水を琿通して Λ量 i を介して水槽 4 に送り 出し、 S方 、 ¾量 0— t- ¾、濃度 o2に *厚化した海 水はタ 一ビン 7へ供縿される · タ 一ビン グ の入口ノ ズThe traditional c banquet of Huo Yi Zhi »is structured as shown in the No. 1 / aa flow chart. The dew / B is an example of seawater in the seawater / 0, which is not shown in the drawing and is unreasonable. rarely, the pump / the discharge pressure, discharge rate, discharge in the Ko麼0 beta, through 8Ξ ChikaraiHajikamiben a be more Seimai the pressure sensing讎<2 * semipermeable membrane * Schlenk f Through the pressure leak point of the fficatosuto SJ *, enter the semi-translucent * confetti, and resist the osmotic pressure by the surface EE force. through and out sent to the water tank 4, S side, ¾ the amount of 0 - t- ¾, * thickened the sea water to a concentration o 2 of-data one bottle grayed to be Kyo縿to the other one bottle 7 entrance Roh's
Λ ル はァクチユエータ Jにより鬭鹰を黼歸される。 タ 一ビン , により裸られる ネルギーはポンプ モ ー タ f を助勢するために用いられる。 The key is returned by the activator J. The energy stripped by the bin is used to assist the pump motor f.
Jfel上の構成においてポンプ / の吐出圧力 は通常 * The discharge pressure of the pump / in the configuration on Jfel is usually *
*の海水の浸透 に対し T " 0ifZc«l で あり、 ポンプ / の吐出量 ¾0の内半透 ¾では 《2ク〜 *ク ¾| * "Is a 0ifZc« l, in the inner semipermeable ¾ of the pump / discharge amount ¾ 0 "T for the penetration of sea water of 2 Qu ~ * click ¾ |
f O PI - が道浸透して莪水化され 。 f O PI -The water has penetrated the road.
上锊に示すように奠分離義置に於いてはポンプ / の 霾力が難常に大きな割食を占めており、 の一《* a 取する為近年厲凼ロ機續 * ¾ E管への動力園驭タ 一ビ As shown in the above section, the haze power of the pump / is inevitably occupying a large part of the eclipse in the perennial separation device. Power Garden
S ン 7、 例えばペル ト ン水車の ¾置が逢められている。 The installation of a Singaporean, for example, a Pelton turbine has been seen.
然し乍らその通転方法は希薄渗截の園枳率のみに着 3 し半透囊 *の最大許審函轵車で ンプ / の軸動力を最 小とするものであった。  However, the driving method was to use only the sparse cut-off rate, and to minimize the shaft power of the pump / semi-transparency * with the maximum permissible inspection car.
発明の顯示  Inventive manifestation
to 背景技術にのぺたように ¾来技術は希薄渗液の國轵 車のみに着 Sし半透腐の最大許容函枳車でポンプの輪 励力を最小とするものであったため動力回取手 «によ つて囫収された ¾力を併せて考盧に入れたものでない ため消費される動力はー毅に最小となるものでなかつto As described in the background art, the conventional technology arrived only on a domestic vehicle with a dilute solution. Since the power recovered by «was not taken into account, the power consumed was not minimal.
" た o "
本発明は廣分離義置においてポンブの所要動力と動 力画驭手 ftの園驭廳方の羞が最小となる如き澳量黼歸 襄 *奁提供する Cとそ S的とする。  In the present invention, it is assumed that the required power of the pump and the power ft of the pump are set to be the minimum in the garden in a large-scale separable storage device.
本発明は囊分讓義置 おいてポンブと動力回驭手& The present invention relates to a pump and a motor
Λ の性攄龜纏 利用し軸動力と回驭勐力の兼、 即ちモ - タ厨 *歸カを最小とする鶬歸肇置を提供することによ り、 最も効.車のよい爭透鎮装置の最大効皐を確保する ものであ ^。 効 効 攄 攄 効 最 も 効 効 効 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 効 最 も 効 効 効 効 効 効 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 効 効 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 最 も 効 こ と こ と 最 も 最 も 最 も 最 も 最 も 最 も 最 もIt is intended to ensure the maximum effectiveness of the equipment.
本発明は半透膜による物質分讓肇置において ンプ の性能曲線と、 動力回枳手段の性能曲線と、 溶液中の  The present invention relates to a performance curve of a pump, a performance curve of a power control means, and
f O I 瀋質の濃度と浸透圧の調係 用いて 定された希薄も し くは纖纏灌液 *量に於ける最小所餐鷉カ *算出する 制輝園路を備えた濃量劁舅勰置を有する裏分鐘襄置で あ f OI Coordination of concentration and osmotic pressure of shenrite Dilute or fibrous irrigation solution determined using * Minimum amount of food in volume * Calculated With a
本驩発明は供 液の加圧励作をするポンプと、 ボ ンブと半透膜 IWの配管中に介在させた £カ龔薑升と、 半透膜と、 半透膜より囊線濂液儒下 に醞した鷉カ國 衩手 βを傪え、 半透膜 用いて渗液中の 質 分譲し 希薄灌濱と濃續滲液を得る腐分讓襄置において、 ボン ブの性鐃翁纏と、 動力園轵手 の性餓曲纏と、 禱讓申 の灌質の湯度と浸透 £の Η係を用いて it定された希薄 もし くは湯纖讓液澳量に於ける最小所餐繳カを算出す る制御回路を備えた 31量制御養置を有する纏分龍襄置 である。  The present invention relates to a pump for pressurized excitation of a liquid, a pump and a semi-permeable membrane interposed in the piping of the IW, a semi-permeable membrane, and a semi-permeable membrane. Using a semi-permeable membrane, the quality of the liquid in the sap is obtained using the semi-permeable membrane. The minimum in the amount of dilute or hot water, determined by using the relationship between the temperature of the perfusion and the permeation of the perfusate of the water, This is a Ryujo rig with a 31-volume control system equipped with a control circuit that calculates the restaurant meal.
最小所長動力が算出されることにより、 最小所要動 力を得る通転点における供 液羝量、 供 液圧力、 囊 禱痕流量、 囊績液圧力、 Cのような癱量、 圧力を定め る カ調薑弁の園康、 勐カ画収手《«ぇばタ ービンの 入口弁 w度が一つの制輝系として一義的に求まる。 ¾ つて針算のみによって算出された圧力詞薑弁の弁鬭度、 タ ービン入口弁麵麼になるように圧力講薑弁、 タ ービ ンを制舞することにより最小所要動力にて通転される ものであり、 次にのべるような E力もし くは ¾量の検 出手《を僮えてこれらの搶出手《の検出條が系内邇膽 圧力もし く は Λ量と等し く なるように圧力講薑升及び  By calculating the minimum director power, the liquid supply volume, liquid supply pressure, trace flow volume, test liquid pressure, volume and pressure such as C at the turning point where the minimum required power is obtained are determined.調 調 薑 園 ぇ 入口 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度鬭 The valve stroke of the pressure ginger valve calculated only by hand counting and the turbine inlet valve are controlled so that the pressure ginger valve and the turbine are controlled so that they run with minimum required power. In order to detect the following E force or a small amount of detectors, the detection conditions of these minors must be equal to the internal pressure or the amount. Pressure
OMFI L一 勐カ園轵 奄調薑することもで奢るものである。 OMFI L 一 勐 カ 園 轵 Amago ginger can also be used.
本躀第 請求項は第 / 請求項において、 ポンプと 半透 SI Mの配管に £力擒凼手 もし くは漉量検出手 A 備え、 &の箱示值が算凼した ϋ表處 於ける供維濱 s の系内理驗圧力もし くは系内珊請 と等し く なる様 に £力調整弁の開度及び動力園 手 ftを調養する黼卿 固路を德えた廣分態装置である。  The claim of the present invention is characterized in that the pump and the semi-permeable SIM piping are provided with a pressure-intensifying means or a strain-detecting means A in the claim / claim and a & box indication is calculated. A wide-spreading device equipped with a pressure regulating valve opening and a power garden hand ft to adjust the opening of the power control valve so that it is equal to the pressure in the system or the system in the system It is.
本躀第 *請求項は第 / 請求項において半透薦と励力 園枳手段 囊纏液の圧力搶出手 Sを備え、 Cの損承 to 僮が算出した濃耱液の系内 ¾敏圧力と等し く なるよう に動力回驭手 ¾もし くは圧力調整弁 糊《する制御函 路を備元た鹛分薩装置である。  The * claim is a semi-transparent recommendation and an energizing means in claim / claim. 手段 囊 圧 力 囊 圧 力 圧 力 圧 力 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え 備 え ¾ ¾ ¾ This device is equipped with a control circuit that provides a power circuit or a pressure regulating valve to make it equal.
本願第 請求項は第 / 請求項において半透廣と動力 園驭手段 Mに饑續液の «量検出手 を僇え、 この掬示 值が算出した *纏液の'系内理請鲺量と等し く なるよう に廳カ回驭手 Sもし くは E力調整弁を制舞する制 路を傳えた鹏分鶴装置である。  Claims of the present application are based on the claims / claims, wherein a means for detecting the amount of the stagnant liquid is provided to the means for semi-transparent and power cultivating means M, and this scooping is calculated. This is a split crane device that conveys a control system to control the power control valve S or E.
本順第 請求項は第 / 請求: ¾において、 半透腐より 希薄澳液優下饞 流量検凼手段を偏え、 この指示值が Claims in this order are claims / claims: ¾ 希 薄 よ り よ り 半 よ り よ り よ り 值 值
Λ 希薄液の系内理 »量と等し く なるように £力謂整弁 もし くは數カ回驭手段を髗舞する制舞回路を備えた鎮 分鐘装置である。 内 This is a separation bell device equipped with a control circuit that performs a so-called valve-regulating or several-time control so that the amount of diluent becomes equal to the volume.
本臞第 7請求項は第 / 請求項乃至第 請求項の何れ かにおいて、 最小所要勐カを算出す *制舞画路が許容The seventh claim is the invention according to any one of the claims / claims to which the minimum required power is calculated.
2S 回収率設定器を備え、 半透廣の許容回収率以下の範囲 で所餐動力が最小とな Equipped with a 2S recovery setter, within a semi-global allowable recovery rate or less And the power of dining is minimal
た膜分雌義置である。  It is a female part of the membrane.
本鑕 ¾ は^上のようにポンプと, 動力 a n手 βと、 ポンブの吐出 £力詞薑弁 *儒えお膜分離養置 おいて、 S ポンプ及び勐カ藺衩手 の性龍幽繡と、 藩質の癱虞と 浸透 £の園保を基に義置の通 範钃内に於ける最低腈 餐動力の通 点を算出することで薦分讓操作で必餐な 數力の大きな «食を占める高圧ポンブの廳カ奁滅少さ せる Cとが出来る効秉を有する。  The main unit is the pump, the power β, and the discharge of the pump, as shown above. Calculating the point of minimum supper power within the standard of the detention system based on the census of the clan quality and the penetration of the garden «The high pressure pump that occupies the food has the effect of making it possible to reduce C.
'0 本願発明の夷鎵纏様項ぼ夫 4r 珊讓液の配管中に £ 力検出手《もし くは集量検出手《を養えその損示值が 系内邐膽圧力もし くは澳量になるように圧力調蓬弁も し くは動力画轵手 を調畫す ものであり、 鷉分讓義 置に 手《と黼御手《を»加するのみで黼歸でき簡'0 In the present invention, the force detecting means (or the collecting amount detecting means) was cultivated in the pipe of the 4r corrosive liquid in the pipe of the present invention, and the loss of the force was detected in the system. In order to obtain a pressure control valve or a power scheme, the procedure is simple.
" 拳で正確な制歸を行う cとの出来る効果を有する。 It has the effect that you can return accurately with a fist.
面の筒単な説明  Simple description of the surface cylinder
解 / は鹏分麵養置のフ ロ ーシ ー ト、 嬉《2 »は膜分 麵儘置の圧力と濂量の讕保を説明する線 8、 第 J 図乃 至露 は膜分鐘義置の所養動力と損失動力を示す線 Solution / is the flow sheet for fermentation, and joy <2 »is the line 8 that explains the pressure and the amount of lipolysis in the film as it is placed. Line showing the power of the plant and the power lost
Λ6 g、 第 4図は本発明の実; M例のブロック図、 第 7図は 簾 4 aの一ブロックを示す纏 siである。 .Lambda.6 g, Fig. 4 real present invention; block diagram of M examples, FIG. 7 is a fireman's standard si showing one block of interdigital 4 a.
発明 実; Mするための最柬の形簾  Invention M
Cこで本発明の実詹 する翁に腐分讓装置の 動力調倮 説明する。 ポンプ / の軸動力、 タ ービン f の Θ釈動力、 *ータ f の所餐動力についてのぺる  C Here, the power control of the device for exchanging rot to young people according to the present invention will be described. Pump / shaft power, turbine f driving power, * f
OMPI 一 ポンプ動力 I·»は OMPI one Pump power I
^ ただし : 7? ポンプ / の効皐 ^ However: 7? Pump / Effectiveness
PL1 ポンプ / から半透膜 * までの圧力属薹并 タ ービン 7の躍秋詹カ は /
Figure imgf000008_0001
) 9ϊ ただし 2 ?τ タ ー ピン 7の効率
P L1 pump / to semi-permeable membrane *
Figure imgf000008_0001
) 9ϊ However efficiency of 2? Τ Turn-pin 7
L2 半透 « * から タ 一ビン 7 の入ロ ノ ズル,、 までの管路の圧力損失 L 2 semipermeable pressure loss of the pipe of up to Nyuro Roh nozzle ,, of «from * data one bottle 7
従って モータ所 S動力 Lは  Therefore, the motor station S power L
1ι― Ιι,一 LF 1ι― Ιι, ichi L F
- , Zf,+ ( , ¾1 "Η^^,Ζ ) + (  -, Zf, + (, ¾1 "Η ^^, Ζ) + (
I>K& - ιριιΖ I> K &-ι ρ ιιΖ
第 ^図は圧力歸養弁によるバルブ £損と希薄液 (褒 水 )澳量等の鼸係を示す線 Sで横軸 ^量、 續職に £ 力:?をとつてある。 幽纏 Aはポンプ / の性飽曲纖 ( A  Fig. ^ Is a horizontal line with a line S indicating the relationship between the valve loss due to the pressure return valve and the amount of dilute solution (recharge water). Is taken. Yuma A is a pump
OMFI 一 H曲練 :)、 曲線 Β,Ο は £力調整弁 Λ 絞った時の鷉 面 力?!!と «面へ供搶される «:! の »保を示すもの である。 曲纏 Β より も曲線 0 は圧力謂養升 を更に « り込んだものである。 OMFI 1 H Curve :), curves Β, Ο are £ force adjustment valve 鷉 surface force when squeezed? ! ! And «to be confined to the surface». Curve 0 is more inclusive of the so-called pressure increase than song summary Β.
曲纏 Α,Β,σ に対応して希薄液流量 と鎮面 £力 の 腾保は曲線 Α',Β·,σ» で表わされる。 两ー ¾量 で系内 ε力を Ε力調整弁 jをも操作して下げるとポンプ / の 通転点は a→u→c→d→e→f と変化し、鎮面では &— Corresponding to the curves Β, Β, and σ, the retention of the dilute liquid flow rate and the surface pressure are expressed by the curves Α ', Β ·, σ ». If the epsilon force in the system is lowered by operating the force adjustment valve j, too, the turning point of the pump / changes from a → u → c → d → e → f.
→c'→A»→e'→ へと変化する。 例えば、 ポンプ性 tt幽 → c '→ A »→ e' → For example, pumping tt
/0 纏 A上の点 4のポンプ / の吐出 E力 P0と E力調整弁 a / 0 Summary Discharge of pump / at point 4 on A E force P 0 and E force adjustment valve a
を絞った時の曲線 G 上の点 d'の縱座標の差? 0—: PMが E 力調整弁 J によるバルブ EE損となる。 ただし ¾fc点 *, tでは圧力調整弁《2は全開しており、 バルブ S損はな い a Difference between the ordinates of point d 'on curve G when focusing on? 0 -: P M is the valve EE loss due E force adjusting valve J. However, at ¾fc point *, t, pressure regulating valve << 2 is fully open and there is no valve S loss a
ここで希薄液流量 一定の時圧力調整弁 Λの W度と モータ所 «»力 I»の w倮そ求める。 提水を 遣するに 必要な *水化動力! ^はポンプ / の箱切 E近傍 ( β が小 さい に半 膜 *の回枳皐が高い :) では膜面 £力 ΡΜは 大であって、 ポンプ / の効車??は小さい Αに大きな値 Here, when the flow rate of the dilute liquid is constant, the W degree of the pressure control valve と and the w of the motor station «» force I »are obtained. * Hydrogen power required to send water ^ Semi-membrane * times枳皐high :) In the film surface £ force Ρ Μ the pump / of the box off E vicinity is small again a large, pump / of efficiency car? ? Is small Α is large
ΛΟ となり、 ポンプ / の圧力を下げるに ¾がい腐面圧力 ¾ が小さ く、 ポンプ / の »率 が大き く なり淡水化動力  When the pressure of the pump / is reduced, the decay pressure becomes smaller, and the »ratio of the pump / becomes larger, increasing the desalination power.
の值は減少する。 然し乍らポンプ / の効車 には極 大が存在し、 使圧、 大¾ 1慎域では低下する為拔水化 動力 ! ^ は再び増加する。 お ¾路の圧力損失分の動力 LVL は圧力調農弁 の攙抗 值 decreases. However, there is a maximum in the pump / effect car, and the pumping power is reduced in the area where the water pressure increases. ^ Increases again. The power L VL for the pressure loss in the circuit is the resistance of the pressure regulating valve.
ど Αί , ΟΜΡΙ に比較して管磨の S抗は I»常に小さい。 E力調薑弁 によるバルブ圧損は據切 £近费では 、 その後一且增 旗し再び となる β 扉ち極大点が存在する。 Αί Αί, ΟΜΡΙ In comparison with Kuma, the S resistance is always small. The valve pressure drop due to the E-force ginger valve depends on the pressure, but after that, there is a maximum point at the β-door, which is flagged once and then again.
ンプ / 、 タ ービン f の効率に起 Sする纜カ損失 Cable loss caused by the efficiency of the pump / turbine f
MIL はポンプ / 、 タ ービン 7夫 の櫬霍圔有の効皐 ft 線の複合であり、 两者の最大効率点近傪で動力損失 M IL pump / is a composite of Kosatsuki ft line櫬霍圔有the turbines 7 respectively, the power loss at the maximum efficiency point near傪of两者
¾¾ は小さ くなり、 の点より圧力が裹 く とも低く i も大きな億となる。 以上説男の如く淡水化動力 ½、縻 絡の £力損失分の動力 L、 ポンプタ ービンの効車に ¾ 小 becomes smaller, the pressure is lower than the point, and i becomes large. As described above, the desalination power ½, the power L T¾ for the power loss due to the chorion , and the effect of the pump turbine
(0 起因する動力損失 I ^共圧力 (扉ち園轼皐) とは单鍵  (0 Power loss due to I ^ co-pressure
な比例調係ではない。 若千の《を第 J 、 第 *驕、 第 r図に示す。 図において横輔は圧力、 緩輔は »力で表 わしてある e  It's not a big proportion. Wakasen's << is shown in Figure J, * Arrogant, Figure r. In the figure, Yokosuke is represented by pressure and Loose is represented by »force.
第 J 図ではモ ータ f の所養動力 I»はポンプ / の吐岀 it E力 が大き く、 S iR車が大きい種小さい。  In Fig. J, the feeding power I of the motor f has a large pump / discharge itE power, and the SIR vehicle is large and small.
第 * B9ではモータ rの所餐動力 Lは囲轵率に無鬭倮 にほぼ一定である。  In the * B9, the power L of the motor r is almost constant regardless of the surrounding ratio.
第 図で 回枳皐(扉ち E力 )の低い方がモータ f の所 ¾勐カ I·は小さ く省動力である。 In the figure, the motor f has a smaller power I at the lower end of the shaft (power E), which is less power-saving.
0 第 J理巧至第 図で示すように藪水化動力 ½は低 £ 大流量域と高圧の栅仓に高 く極小値が中闥の園轵皐の «分に存在する。  0 As shown in Fig. J, the hydration power 高 is high in the low-low flow area and high-pressure area, and its local minimum value is located in the middle of the garden.
¾路の E力損失分の勳カ 31失 Lはポンプ / の吐出 圧力 の增加と共に增加して再ぴ滅少し極大威を有す Λ る。 ポンプ / 、 タ ービン 7の効率に起因する損失黼カ The power loss of the E-force in the circuit, which is lost 31 Lt, increases with the increase of the discharge pressure of the pump / and is extinguished . Loss due to pump / turbine 7 efficiency
OMPI Ι ΙΙ» は低滅 «Λであり、 ポンプ / の吐出 EE力減少と共 に滅分を滅少させる。 OMPI Ι ΙΙ »is depleted« Λ, and the depletion is reduced together with the decrease in the pump EE discharge force.
以下本発明の実 *例 *第 488の鹪 Λブロック Sによ り SRWする。  Hereinafter, SRW is performed by the 488th block S of the present invention.
先ず希薄液《量 を希薄液 Λ量《定》 / ク に入力す る · 許容画织車我定》 / / により許容最大回枳皐  First, enter the amount of diluted liquid in the volume of the diluted liquid.
を求める。  Ask for.
許審園釈率 IK定 S / / からの出力の許容最大回驭搴 RMAX 及び希薄液濂量股定舊 / からの出力の希薄液 to 流量 を暈小^液量演算 S / に入力して最小翁液量  Input the permissible maximum rotation of the output from the IK set S // and input the dilute R to the flow rate of the dilute liquid from the output of the set / Minimum volume of liquid
¾Ο«Μ = <¾Ι/¾ΑΧ を算出してポンプ性餞曲纏 Aの戮数調 倮を予め £«させてある »数発生 S / Jに入力し最小  Calculate ¾Ο «Μ = <¾Ι / ¾ΑΧ and enter the number of the pre-punched 曲 曲 曲 of A
液量 に見合う最大吐出 £力 mi を出力して 最大圧力演算 S / * に入力する。  Output the maximum discharge pressure mi corresponding to the liquid volume and input it to the maximum pressure calculation S / *.
" 希薄液流量 からこの ¾量 ,に見合う最大吐出圧力 "Maximum discharge pressure corresponding to this flow rate from dilute liquid flow rate
Poiuxa を求めるのであるがここで第 図を薩れて希薄 液 mm から、 膜に供 される吐出量^を求める方法 をのぺる O  The Poiuxa is obtained. Here, the method shown in Fig. 10 is used to calculate the discharge amount ^ supplied to the membrane from the dilute liquid mm.
(1) ポンブ / の吐出圧力 が返定される。 ポンプ吐出  (1) The discharge pressure of pump / is returned. Pump discharge
EE方 Ρβを 定するとポンプ性能曲線 Aからポンプ / の吐出量^が求まる。 If the EE method Ρ β is determined, the pump performance curve A will be used to determine the pump / discharge rate ^.
(¾ 纖纏液 ¾鼂 一 であるから項目 ωにおいて  (¾ 項目 纏
求めた βから設定僮の ,を滅ずると求まる。 From the obtained β , it can be obtained by extinguishing, in the set child.
(3) 浸透圧 と海水濃度 CMの黝保は一義的である。 半 (3) The osmotic pressure and seawater concentration C M The shaking of C M is unique. Half
透鶬 の供給俸の液濃度 GMは廣入口液の澳度 CQ、 濃 Liquid concentration G M supply salary of Toru鶬is澳度C Q of Hiroshi inlet liquid, concentrated
O PI O PI
0 O 縮液濃度^とすると近俱的 ^^(Ca + ^)/^で定ま る。 Ge ,C¾ は ¾驭皐 著し く变化しない »り、 上 g近似式でよい。 ¾つて又 , は春 裏置の通 常邁 申は定歡とみなすことができる β この 91係か ら浸透圧 *Μが求まる。 Treasure 0 O If the condensate concentration is ^, it is determined by the following formula: ^^ (Ca + ^) / ^. G e , C ¾ does not change well. ¾ connexion Further, the spring Ura置normal邁monkey It can beta Micromax is obtained this 91 engaging either et osmotic * regarded as Tei歡.
(4) 供搶海水が置度変化の著しいときには供籍偏 £管  (4) When the seawater has a significant change in the water level, the distribution center is
中の供翁液重度を検出する置度梭凼墨を け ただし 腐の霍截により定まる常数  Use the ink to detect the severity of the liquor in the liquid, but the constant determined by the rot of rot
/0 ^ 囊内の水の拡散保数  Diffusion coefficient of water in / 0 ^ 囊
τ 液め置麼  τ liquid
により保数 Ϊを算 ffiする。 液の量废変化が小さい 場食には定数としてよい。  Calculate the retention Ϊ by A constant value may be used for small meals where the amount of liquid / change is small.
m 半透膜 *の供 *圧力? Mは項 s u)で《定したポン m Semi-permeable membrane * pressure * pressure? M is the term
ブ · の吐出 E力 ΡΒから半透廣 * までの供給儒配管の ¾体の EE力調薑弁 aを含む管路による損失へッ ドHead discharge E force of the probe · [rho from Β to losses due conduit containing EE Chikaracho Hajikamiben a of ¾ of the supply儒配pipe to HanToruHiroshi *
¾t そ *じたものである。 半透厲 f の希薄資£力?, はほぼ一定であり、 又希薄液囊虞は一定とみてよい から希薄液の浸透 E*,は一定としてよい。 そこで道¾t It is the same. Semi-transparent f's diluted capital? , Are almost constant, and the dilute solution can be considered to be constant, so that the penetration E * of the dilute solution may be constant. There road
20 20
を算出する。 Is calculated.
(® 希薄液 Λ量^は半透膜の膜面積を とすると  (® Dilute volume Λ volume is the membrane area of semipermeable membrane
ΜΚΔ · · · · ( ) ~ Α Μ ΚΔ
2S で表わされる。 半透膜 4»の希薄餐流量が浸透 £を越  It is represented by 2S. Semi-permeable membrane 4 »dilute flow exceeds penetration £
f Ο ?1 - える SE力 Ρ により ¾化する希薄截 i は一次比 例である。 式 ωにより針算した 1¾ 0AL0とする。 f Ο? 1- The dilute i, which is degraded by the SE force え る, is a first-order specific example. 1¾0AL0 calculated by the formula ω.
(7) 設定した と を比 «!する。 そして Cの »差 が大きいときは項 S ) 夏りポンブ吐出 ΑΕΡβを再 «(7) The set and are compared. And if the difference of C is large, the term S) summer pump discharge ΑΕΡ β
JT 定して項黼 (1)へ (7)そループにしてく りかえし、 <¾1と JT is specified, and then to clause (1). (7) The loop is repeated.
dlOAI.0の麟差がは!になるまでく り す。  The difference of dlOAI.0 is! Until it becomes.
ここで第 J理で示すように最大の希薄 **量 <¾ ! 3t に对応するポンプ / の吐出 ε力 , よりも先に項 B )で «定した £力^が小さい箱騙で <¾10AiO-¾1 >^な Here, as shown in the J theory, the pump / discharge ε force corresponding to the maximum lean ** amount <¾! ¾10AiO-¾1> ^
10 るときは再 «定の を最初に «定した P0より も小さ く し、 — く なるときは再 «定した∑»βは最初 に «定した ρ0よりも大き くする。 10 Rutoki re «to rather smaller than the first« boss was P 0 constant of the, - when Ku becomes re «boss was Σ» β is larger than the first in «boss was ρ 0 Kusuru.
最初に項 g (i)で返定したポンプ / の吐出 £力 が 希薄《Λ量 ¾11UX に対応するポンプ / の吐出圧力? (MThe discharge pressure of the pump / returned in the first term in g (i) is low. (M
" より も大きい範鼴で CAL0一 > なるときは再 «¾ の!》βを最初に《¾した Ρβより も大き く し、 i< L0 — <¾,<ク になるときは再 定の?βを最初に «定した よりも小さ <す 。 "CAL0 one> made when a large range鼴than re« of ¾! "To first to" much larger than the Ρ β was ¾ β a, i <L0 - <¾, is when it comes to <click of re-constant Β is smaller than originally set.
m »定した希薄液 *量 と項 s (i)〜mまでにおいて m »Specified dilute liquid * volume and terms s (i) to m
^ 針算した ^ CAL0 との差である針算麟差が許審值 内 であれば仮定したポンプ吐出 E力 を正しいとする。 希薄液 Λ量 を》定するとポンプ / の性鉋曲線が定 まっており、 かつ灌液の種類により機度と浸透圧の^ If the needle difference, which is the difference from the calculated ^ CAL0, is within the permissible range, it is assumed that the assumed pump discharge E force is correct. When the diluent volume is determined, the pump / property curve is determined, and the degree of osmotic pressure and the degree of osmotic pressure depend on the type of irrigation fluid.
»係も定つているのでポンプ / の吐出 Ε力? aと希薄 液 Λ量 の 保は一義的に決定される。 ¾つて上述 した項 8 〜mの手龎は数值表として編めることに より省略でき 。 »Since the staff is also fixed, the pump / discharge power is high? The preservation of a and the amount of diluted liquid is uniquely determined. About the above Steps 8 to m above can be omitted by weaving them as a mathematical table.
又闻一ぬ希薄液 ¾量 於いて第 a aに示すよう に二種鎖のポンプ / の吐凼压 が求まる。 E力の高 In addition, in the case of a very small amount of diluted liquid, the discharge of a double-chain pump is determined as shown in a. High E power
* い方蚤? tHAXZ、 い方 ?omi とする。 * Is this a flea? tHAXZ, which is? omi.
第 A 図に蔑って巍興する。 希薄液%量設定》 / の 出力は 〜 ^数発生器 / に入力される。 そして闢 数 S生優 / の内赛は第 7顧に横轅 希薄痕 量 、 編轅にポンプ / の吐出 £力 Ρβ¾示し、 希薄液の 3 幽 t 纏を表わす鐮 8もし くは相裹する数爽を E億させてあ Wexing, disdaining Figure A. The output of "Dilute liquid% setting" / is input to ~ ^ number generator /. The number of S / Y / s is the amount of dilute traces of Yokouen in the seventh column, and the discharge power of the pump / is shown in Zhengyuan, β , and represents the depth of the dilute liquid. Let the number of linings be E billion
り、 希薄液 ¾量 を入力するとポンプ / の吐出圧力  When the volume of the dilute liquid is input, the discharge pressure of the pump /
ΡβΜΑΖ2 , ?0XXir を凼カするようになつている。 最大ボン ブ吐出 EE力 ΡαΜΑχιは最大 Ε力演算器 / *に入力する。 ポンプ性餓曲鐮から求めたポンプ / の吐 ¾S力 ^HAZi は半透囊 *の性状から定まる最大 E力であり、 希薄液 ¾量 とポンプ / の吐 ¾量の 81保から求めたポンプ / の吐出圧力 はポンブ性鉋から定まる最大圧力で ある。 それ故義置として許される最大 E力は ΡβΜΑΙ, , ?βΜΑΖ2 の内小さい方の值であり、 最大圧力演算 S / # は E力 P0KAX, を比較して小さい方の值を ¾力す も。 れを ^ΟΜΑΖとする β Ρ β ΜΑΖ2,? 0 XXir. The maximum bomb discharge EE power ΡαΜΑχι is input to the maximum power calculator / *. The S / S power ^ HAZi is the maximum E force determined from the properties of the semi-permeable *, calculated from the pumping curve, and the pump / Is the maximum pressure determined by the pumping plane. Therefore, the maximum E force allowed as a prosthesis is the smaller of Ρ βΜ ΑΙ ,,? Β ΜΑΖ2, and the maximum pressure calculation S / # compares the E force P 0KAX , and finds the smaller 值I'll do it. Where ^ ΟΜΑΖ
吐 ¾Ε力演算 S / 4には最大 £力《算》 / *の a力 である圧力
Figure imgf000014_0001
数発生 S の出力で ある圧力 が入力される。 そして濱算 «»|»定》 t 7にて設定してある演算 1WSI Nが入力され、 Λえば
Discharge power calculation S / 4 has a pressure of a force of a maximum of £ power / *
Figure imgf000014_0001
Pressure, which is the output of number generation S, is input. And Hamasan «» | »constant" operation 1WSI N, which is set at t 7 is input, if e Λ
ΟΜΡΙ 等 MSIにて Semi〜: ΡβΜΑΐ W 分構して ( /ΖΜ) ΟΜΡΙ At MSI Semi ~ : Ρ β ΜΑΐ W (構 / ΖΜ)
?0 W = C /Ti ) C PQMAZ - ^ΟΜΧ» ) + P0MIJI? 0 W = C / Ti) C PQMAZ-^ ΟΜΧ ») + P 0MIJI
Figure imgf000015_0001
Figure imgf000015_0001
なる針算が行われ、 これらの錶条はマルチプレクサ These calculations are performed by a multiplexer.
/ に入力される。 マルチプレクサ / f から属 Λ出力 されも ^ )〜: p,wを受けたポンプ性錢龜纏及びポンブ 動力の鼸数発生》 / f では入力の E力 ( 〜 :Ρβ(8)に見 t 食う吐凼量 <¾e = f(P0 ポンプ吐凼量 に見食うポンプ / の所鋈 »力 を ¾力する。 そして ータ所 餐動力演算器 a / にポンプ動力 が入力され、 囊纏液 濱算》 Λ 2にポンプ性饞曲線及びポンプ動力の属 数発生 » / f からのポンプ / の吐出量 βが入力される。 ft 囊纏痕澳量演算躉 a aは希薄液流量 19;定 S / から の入力の希薄痕 *量 <^から濃續液流!: ¾2=¾β-¾1 を演 算して出力の濃舊液 Λ量^ タ 一ビン 7の性饞曲線の W数発生 S J、 湯廣濱算鏐 *に送る。 機麼演算 β ュ *はポンプ性鉋曲纏と動力特性線の調数発生》 / fEntered into /. Multiplexer / f also generates output ^) ~: p, w receives pump power, and generates pump power》 / f, input E force (~: Ρ β (8) eat吐凼amount <¾ e = f (P 0 pump吐凼amount to ¾ force the Tokoro鋈»force of the pump / eats seen. Then over data plant餐動force calculator a / the pump power is input,囊纏. liquid Hamasan "discharge amount of the pump / from the genus incidence» / f of the pump of饞曲lines and pump power to lambda 2 beta is inputted ft囊纏mark澳量operation躉aa dilute solution flow 19; constant Dilute mark of input from S / * Concentrated liquid flow from volume <^: Concentrated liquid of output by calculating ¾2 = ¾β- 出力 1 , Sent to Yuhirohama **.
ΛΟ からのポンプ / の B W量 0が入力されており、 濃續液 濃廣 ca = oex e / を針算して、 震面濃度 0M=(00+ CA) を算出して出力し、 浸透 £の »敷発生》 a i "に入 力する。 該 M数発生器 *3 は浸透 £ ^-f(OK)の鬭数か ら «.a s»M 出力して圧力演算 β ·2 に入力する。 £ 方演算 4 には囊纏液流量濱算 β ·3 から漫續痕流 The BW volume 0 of the pump / from ΛΟ is input, and the concentration of the continuation liquid, c a = o ex e /, is added to calculate the seismic surface concentration 0 M = (0 0 + C A ). Output, and input to the penetrating £ »floor generation» ai ”. The M number generator * 3 outputs« .as » M from the permeation £ ^ -f (OK)) and calculates the pressure β · Input to 2. In the formula calculation 4, the continuous trace flow is calculated from the
OMPI i<%iをそして希薄象 X量 定爆 / から希薄液流量^ を入力してお!?、 鎮面 E力 を針算する。 そして半透襄 *からタ ービン の入ロノ ズル 'までの管絡の損失水頭 Ρ¾2 を次式で求める。 C 、で ^は管路 より定まる常数 OMPI Enter i <% i and dilute elephant X amount. ? Calculate the E-force. Then, the head loss 管 ¾2 of the conduit from the semi-transparent sho * to the turbulent nozzle is calculated by the following equation. C, where ^ is a constant determined by the pipeline
は管路の規定《量  Is the regulation of the pipeline
そして濃績液 £力 -
Figure imgf000016_0001
¾2がタ一ビン 7へ供 され t る液体の £Ε力である 0 Cの練果の濃纏液圧力 は £力 演算 4から出力されてタ 一ピン性鉻曲纖の讕数 H 生 に入力され、 Rに入力されている濃續¾¾量 2とからタ ー ビン発生動力
Figure imgf000016_0002
,?2) «■算 して 出力し、 翁述したモ ー タ所 ¾»力演算》 / に入力す
And concentrated liquid £ power-
Figure imgf000016_0001
The concentrated liquid pressure of 0 C, which is the pressure of the liquid to be supplied to the bin 7 ¾ 2 is supplied to the bin 7. The turbine generation power is calculated from the continuous amount 2 input to
Figure imgf000016_0002
,? 2 ) «Calculate and output, and input to the previously described motor
" も。 " Also.
モ ータ所長詹カ濟算》 J / はモ ー f の所餐勖カ ι· を翳 入力されているポンプ /の所餐動力 からタ 一 ピン 7により回衩された動力 を滅じて求め、 狭モ ー タ f の所養動力 I»を最小動力演算 に送る。 最小 動力演算 · Λ 7は 1-ク,,, 《2 · · · · Hを入力され ると ¾僮し、 レク ト儻号そマルチプレクサ / f に送 り、 L ( i + / ) を上述鬨様に求める。 そしてモ ー タ所 餐動力列 L ( 〜 L I)までを演算して暈小詹カ „を求め る。 この最小勖カ を求めるまで点線で匪まれた镧 歸ブロッ ク では H + / Θの演算がく り通 Sれる β Motor director's calculation >> J / overlooks the restaurant power of motor f and obtains the power of pump / input from the input power of pump / Then, the training power I »of the narrow motor f is sent to the minimum power calculation. Minimum power calculation · 7 is 1-,,, << 2 ··································································································································· L (i + /) Ask. Then, the motor power train L (to LI) is calculated to find the dimming 暈 ま で 镧 こ の こ の ま で ま で ま で 勖 勖 で は で は 求 め る 勖 求 め る で はBe able to pass through β
ΟΜΡΙ 最小廳カ濱算醫 にて算出した最小動力 ¾Μにな るポンプ / の吐 ¾量 ^、吐出 s力? βは m入口弁 »废濱 算器 Λ おいて ΟΜΡΙ The minimum power calculated by the smallest cabin calculus, pump / discharge rate ^, discharge s power? β is the m inlet valve »Takahama
1雄 一 ΡΜ一 1 Τ + Ρ1ι 1 »1 Yuichi Ρ Μ one 1 Τ + Ρ 1ι 1 »
r ただし ¾ 力靄薑弁 の圧力損失 r However, the pressure loss of the 靄 靄
?1,1»: 澳路の圧力損失  ? 1,1 »: Pressure drop in Macau
とすると ^^^ (^/^!^ は規定澳量、 は常《 で求まるか  Then ^^^ (^ / ^! ^ Is stipulated by the amount,
Jihi7 ^^ΐιΐ一 ^ny J ihi7 ^^ ΐιΐ 一 ^ ny
で求められ、 圧力調整弁 4の 〔灣量保数 〕 CTは ただし z' S定数 And [Turning volume] C T of pressure regulating valve 4 is z 'S constant
で求められ ¾βは JRに定まっているから、 £力調整弁 の弁開度は で求められる。 Cのような演算が行われて、弁開度 AT1 が出力されて H示されないサーボ機構により弁ス ト ロ 一グ奁露蒙す *。 Sought is ¾ beta in because they definite to JR, £ valve opening force adjusting valve than is required. An operation similar to C is performed, and the valve opening A T1 is output, and the valve mechanism is exposed by a servo mechanism that does not indicate H *.
タ ービン入口弁顯直濱算》 Λ ,は最小勐カ演算 n Turbin Entrance Valve Naohama Calculation >> ,, is the minimum power operation n
Λ f において針算された最小動力 „に見食う濃縮液 圧力 、 ¾量 2からタ 一ビン入口井 Jの升麵麼 A を から求める。 こ 、 でな S常敷 From the minimum power calculated at f, the concentrated solution pressure and the volume 2 of the concentrated liquid pressure, the amount A of the vial inlet well J is determined from the following equation.
重力の加速盧  Acceleration of gravity
である。 かぐして弁 竅 A72 ¾タ 一ビン入口弁開盧演 算 f は凼力して H示されないサーボ機構を介して ノ ズル ^の弁ス ト ロ ークを調整する。 It is. Kagurashi Bengou A 72 Pota One bin inlet valve opening The calculation f adjusts the valve stroke of the nozzle ^ through a servo mechanism not shown.
実; Ni iにおいては第 図の裏入口弁顯度濱算讎 4 t の凼力の弁画康 At, を EE力調整弁 jの弁ス ト o —タを s サーボ機構で調整するとしたが、 第 / Hのように圧力 Real; in Ni i Bence preparative o Beqa Kang A t, the EE force adjusting valve j of凼力the back inlet valve Akirado Hama San讎4 t of the Figure - was adjusted by the motor s servomechanism But the pressure as the first / H
漏定点 の £力 ¾が算¾值と一致するように SE力横 ffi » 2 »により Eカ講整弁 aを觎歸してもよい。  The E-force regulating valve a may be returned by the SE force lateral ffi »2» so that the force at the determination point matches the calculation.
又 H it lにおいては第 4 ¾のタ ービン入口弁開度濱 算 f の出力の弁 »度 AT a により タ 一ビン入口ノズ The H it l a 4 ¾ of turbines inlet valve opening Hama calculated valve »degree A T a by motor one bottle inlet nozzle of the output of f in
/0 ル^の井ス ト ロ ークを詞整するよう したが濃績液  / 0 Trimmed the well stroke of Le ^
力 を換出する £カ検凼 S (不図示 )を半透膜 *から 勐カ回収手就までの閱に備えて鎵圧力梭出黌の梭出圧 カ^が最小動力 Lmi*における濃縮液 力 になるよう に誼圧力搶出》により動力回驭手 «を制歸してもよい * 供^液配管中に BE力検出器 a »を備えもし くは濃纏 液配管に カ检 ¾ S (不図示 )を像えて EE力調整弁も し くは励力画轵手 Sを暈小動力となるように劁脚する ことは又これを ¾量に置き変; tてもよい。 従ってボン プ / から半透臃 *に到る配管の ¾量検出手 備え、 In order to prepare for the process from the semi-permeable membrane * to the recovery of the power, the pressure of the pressure from the semi-permeable membrane * (not shown) is reduced by the minimum power L mi *. The power recovery device may be driven back by the pressure generator to obtain hydraulic power. * A BE power detector a »is provided in the supply pipe or the power supply pipe is connected to the concentrated liquid pipe. It is also possible to displace the EE force adjusting valve or the exciting force S so as to provide a small amount of power by imaging the EE force adjusting valve or the exciting force S (not shown). Therefore, provision is made for detecting the volume of piping from the pump / to the semi-permeable *
00 該》量検出手 の楠出した供 液の流量が暈小動力に  00) The flow rate of the liquid discharged from the volume detector is
見合う供給痕^量になるように £力 W薑弁 >2及び動 画驭手《を謁整するようにしてもよ く、 半透鎮 *の出 口から動力回枳手 ¾までの饞總液の配管の ¾量梭出手  Audience may be applied to the wedge valve> 2 and the moving picture so that the supply mark may be appropriate.The total liquid from the outlet of the semi-transparent * to the powering hand Large number of pipes
を備え、 該濂量検出手 の検出した濃績液の%量が 最小動力に見合う纖續液 ¾量になるように圧力調整弁  And a pressure regulating valve such that the% amount of the concentrated liquid detected by the fiber amount detecting means is a fiber liquid amount corresponding to the minimum power.
Λ^ J及び励力回甎手 « 調麄するようにしてもよい。 貴業上の利用可濂性 Λ ^ It is also possible to adjust the J and the excitation power. Available for your business
本発明では特に海水の戴水化のよう 大動力 ¾·必餐 とする場食に遣するが、 一 Kにその他薬 A、 食&等の 纖等に用いられる。  In the present invention, the food is sent to a table meal, which is a must-have meal, especially for the ingestion of seawater, but 1K is used for other medicines A, food and other fibers.

Claims

請 求 の 範 H ι 供維禱液の加 作 *す ポンプと、 ポンプと半 透薦颶の配管中 介在させた £力調薦弁と、 半透鎮 と、 半透臓より濃績渗懷儒下集に配した詹カ闥釈手 を備え、 半透腐を用いて清液中の藩質 分鐘し希 薄禱滅と囊績澳概を得る蠤分觎義置 おいて、 ボン ブの性餞義纏と、 詹カ豳较手 ftの性攄龜線と、 潜液 中の清貧の濃魔と浸透圧の M保を用いて 定された to 希薄もし くは濃纏溶痕澳量に於け 最小朥餐励力 算凼する制簿圈絡そ铺えた魔量 M御義置を有する讓 分離肇置。 Scope of request H ι Operation of the supply liquid * Pump, pump and pressure regulating valve interposed in the piping of the pump and semi-transparent storm, semi-transparent membrane, and higher performance than the semi-transparent organ It is equipped with a hand-painted knives arranged in the Confucian Confucianism.餞 餞 餞 と 、 詹 ft to to to to to to ft to to ft to to to At the moment, the minimum amount of encouraging power is calculated.
よ ポンプと半透簾 Wの配管に圧力検 ¾手《を備え、 この掬示儘が算出した運転点に於ける供給液の系内 " 理請圧力と等し くなる様に圧力謂整弁の調鹰及び動 方園轵爭 を調薑する制御回路を備えた請求の範囲 第 t項 C麟の讓分薩襄置。  The pump and the semi-transparent W pipe are equipped with a pressure detector, and the pressure is regulated so that it becomes equal to the control pressure in the supply liquid at the calculated operating point. Claims comprising a control circuit for controlling the operation of the device and the operation of the device.
^ ポンプと半道腐 !¾の K管に ¾量検出手《を俵え、 この招示爐が算出した運転点 於ける供 液の系内 ^ The pump and the semicircular rot! 腐 pipe can be weighed with the mass detector, and the furnace is operated at the calculated operating point.
Λ 理請澳量と等し く なるように圧力謁薑弁の M廣及び 動力回枳手 を謂建する制御鼸路を儍えた請求の箱 囲第 /項 E の廣分譲襄置。 請求 The billing box in section / E of the billing box with a control circuit for the so-called "M" of the pressure gauge valve and the power circuit so as to be equal to the quantity of the request.
* 半透虞と動力國驭手 Mに津耱観の £力検出手 そ葡え、 この搛示值が算出した: 1転 に於ける演續 液の系内理膽圧力と等し くなるように動力園较手 ¾ もし くは EE力調養弁を黼譚する制御回路そ偏えた請 求の錄囲第 /項 ε載の薦分膽義置。 * Semi-permeability and power 驭 驭 M M £ 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛 搛Power Garden Or, a control circuit for controlling the EE power regulating valve.
Λ 半透膿と動力回驭手緻 Μに濃續液の X量検出手  半 Semi-permeability and power recovery
を儒え、 この指示值が算凼した運転点に於ける囊纏 s 液の系内現請澳量と等し く なるように動力闥驭手 IT  In order to make it equal to the current amount of liquid in the system at the operating point calculated by this instruction,
もし くは圧力興整弁を制輝する制御函路を僕えた I* 求の範騰第 / 項 E戴の腐分賺襄置。  In addition, the control box that controls the pressure squeeze valve is controlled.
4 半透鹛より希薄灌液儒下《に«量搶凼手 Aを備え、 この損示億が算出した通 に於ける希薄液の系内 鼉講澳量と等し く なるように圧力調整弁もし くは詹 力回驭手 を制歸する制卿回路を備えた請求の範顧 第 /項 E擊の膜分譲義置。  4 With semi-permeability, equipped with dilute irrigation liquid A, and adjust the pressure so that the loss amount is equal to the calculated amount of diluent in the system. Refer to claim with provision of a control circuit to return the valve or power recovery device.
1 最小所 41動力を算出する制歸回路が許專園轵車 »  1 Minimum location 41 Return circuit to calculate power is a car
定肇を像え、 半透膜の許容豳甎車以下の範園で所要 動力が最小となる ¾義点を算 する機錄を備えたこ と «徹とする請求の範 β第 / 項乃至第 項 Ε戴の 内何れか /つの奠分麵装置。  In the image of Sada Hajime, it is equipped with a function to calculate the meaning point that minimizes the required power in the area below the allowable size of the semi-permeable membrane. Item / One of the periameter devices.
00
¾ ATlO ¾ ATlO
PCT/JP1983/000311 1983-09-19 1983-09-19 Membrane separator WO1985001221A1 (en)

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FR848414385A FR2551989B1 (en) 1983-09-19 1984-09-19 MEMBRANE SEPARATOR

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011083741A (en) * 2009-10-19 2011-04-28 Kyb Co Ltd Seawater desalination apparatus

Citations (4)

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Publication number Priority date Publication date Assignee Title
US3405058A (en) * 1964-02-17 1968-10-08 Wendell S. Miller Purification of water
JPS574286A (en) * 1980-06-11 1982-01-09 Agency Of Ind Science & Technol Method for starting of desalting device by reverse-osmosis method provided with energy recovery device
FR2492470A1 (en) * 1980-10-20 1982-04-23 Stanford Res Inst Int ENERGY RECOVERY DEVICE, MOTOR PUMP FLUID PUMP APPARATUS, AND TYPE ENERGY RECOVERY METHOD USING THE DEVICE AND APPARATUS
JPS58166904A (en) * 1982-03-30 1983-10-03 Kurita Water Ind Ltd Membrane separator

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Publication number Priority date Publication date Assignee Title
DE2917058C2 (en) * 1979-04-27 1982-04-22 L. & C. Steinmüller GmbH, 5270 Gummersbach Single or multi-stage process for desalination or partial desalination of water using reverse osmosis
US4367140A (en) * 1979-11-05 1983-01-04 Sykes Ocean Water Ltd. Reverse osmosis liquid purification apparatus
GR75052B (en) * 1981-01-05 1984-07-13 Mesple Jose L R

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3405058A (en) * 1964-02-17 1968-10-08 Wendell S. Miller Purification of water
JPS574286A (en) * 1980-06-11 1982-01-09 Agency Of Ind Science & Technol Method for starting of desalting device by reverse-osmosis method provided with energy recovery device
FR2492470A1 (en) * 1980-10-20 1982-04-23 Stanford Res Inst Int ENERGY RECOVERY DEVICE, MOTOR PUMP FLUID PUMP APPARATUS, AND TYPE ENERGY RECOVERY METHOD USING THE DEVICE AND APPARATUS
JPS58166904A (en) * 1982-03-30 1983-10-03 Kurita Water Ind Ltd Membrane separator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011083741A (en) * 2009-10-19 2011-04-28 Kyb Co Ltd Seawater desalination apparatus

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FR2551989A1 (en) 1985-03-22
FR2551989B1 (en) 1989-01-27

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