JPS59222222A - Apparatus for discharging quantitatively slurry - Google Patents

Apparatus for discharging quantitatively slurry

Info

Publication number
JPS59222222A
JPS59222222A JP9542283A JP9542283A JPS59222222A JP S59222222 A JPS59222222 A JP S59222222A JP 9542283 A JP9542283 A JP 9542283A JP 9542283 A JP9542283 A JP 9542283A JP S59222222 A JPS59222222 A JP S59222222A
Authority
JP
Japan
Prior art keywords
slurry
discharge
valve
pipe
introducing
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.)
Granted
Application number
JP9542283A
Other languages
Japanese (ja)
Other versions
JPH0347891B2 (en
Inventor
Hirotsugu Ogawa
小川 博嗣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP9542283A priority Critical patent/JPS59222222A/en
Publication of JPS59222222A publication Critical patent/JPS59222222A/en
Publication of JPH0347891B2 publication Critical patent/JPH0347891B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/02Feed or outlet devices therefor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To discharge quantitatively a high-concn. slurry from a high-pressure reactor, etc. by connecting a quantitative vessel to a high-pressure vessel, accumulating the slurry in the vessel in the first place, and then discharging. CONSTITUTION:The slurry is introduced into a quantitative vessel 4 through an introducing pipe 11 having an introducing valve 1. After the quantitative vessel 4 is filled with the slurry, the introducing valve 1 is closed and a discharge valve 2 provided to a discharge pipe 12 is opened to discharge the slurry. After the discharge valve 2 is opened, a gas valve 3 of an introducing pipe 13 for introducing a compressed gas is opened. The remaining slurry is completely discharged by sending the compressed gas.

Description

【発明の詳細な説明】 本発明は、スラリ一定量排出装置に関し、その目的は、
高圧反応装置等から、高濃度のスラリーを定量的に排出
することにある。高濃度のスラリーは、含水率、圧縮率
等の変動で、スラリーの流動特性が不安定なため、バル
ブの開度の調節で排出量を決めることは非常に困難で、
特に高圧の装置からのスラリーの排出はバルブの開度を
小さくする必要」−、スラリーの閉塞が不規則に起り、
事実上、定量排出は不可能である。従来は開口面積の大
きいボールバルブを数分の1秒の単位で全開、全開を周
期的に操り返してスラリーの排出を行ない、その排出量
は、開時間と閉時間の比で調節しているが、排出量はス
ラリーの性状に影響されるため不安定である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for discharging a constant amount of slurry, the purpose of which is to
The objective is to quantitatively discharge high-concentration slurry from a high-pressure reactor or the like. Highly concentrated slurry has unstable flow characteristics due to fluctuations in water content, compressibility, etc., so it is extremely difficult to determine the discharge amount by adjusting the valve opening.
In particular, when discharging slurry from high-pressure equipment, it is necessary to reduce the opening of the valve.
In fact, quantitative discharge is impossible. Conventionally, slurry is discharged by periodically opening and closing a ball valve with a large opening area in units of a fraction of a second, and the amount of discharge is adjusted by the ratio of the opening time to the closing time. However, the discharge amount is unstable because it is affected by the properties of the slurry.

本発明においては、高圧容器に定量容器を接続し、これ
に一旦、スラリーをためてから、排出するので、1回の
排出量は、この定量容器の容積で決まり、スラリーの性
状には影響されることなく、1回の操作で排出される量
は一定になる。この定量容器にスラリーの導入、排出を
操り返すことによって、連続的にスラリーを排出するこ
とができ、排出量は定量容器の容積と、導入、排出の周
期を変えることによって調節することができる。
In the present invention, a metering container is connected to a high-pressure container, and slurry is stored therein and then discharged. Therefore, the amount discharged at one time is determined by the volume of this metering container, and is not affected by the properties of the slurry. The amount discharged in one operation is constant. By controlling the introduction and discharge of the slurry into the metering container, the slurry can be discharged continuously, and the amount of discharge can be adjusted by changing the volume of the metering container and the period of introduction and discharge.

本発明の実施例につき図面を用いて説明すれば、第1図
において、スラリーは、導入弁1を有する導入管11を
経て、定量容器4に入る。スラリーが定量容器4に満た
された時点で導入弁は閉じ、排出管12に設けた排出弁
2が開きスラリーは排出される。ここで、排出弁2を開
いた後の定量容器の圧力は低下するので、スラリーの排
出が不充分なため、排出弁2が開いた後、圧縮ガス(通
常は空気)導入用の導入管13のガス弁3を開き、圧縮
ガスを送って、残留スラリーを完全に排出し、全部の弁
を閉じてlサイクルが終了する。
An embodiment of the present invention will be described with reference to the drawings. In FIG. 1, slurry enters a metering container 4 through an inlet pipe 11 having an inlet valve 1. In FIG. When the metering container 4 is filled with slurry, the introduction valve is closed, and the discharge valve 2 provided in the discharge pipe 12 is opened and the slurry is discharged. Here, since the pressure in the metering container decreases after the discharge valve 2 is opened, the slurry is not sufficiently discharged. The gas valve 3 is opened, compressed gas is sent, the residual slurry is completely discharged, and all the valves are closed to complete the 1 cycle.

第2図は各回の開閉の時期を示したもので、空白が開、
斜線が閉である。先づ、導入弁が開き、スラリーが入っ
た後、導入弁が閉じ、次に排出弁2が開き、スラリーを
排出する。この間にガス弁3が開き、圧縮ガス、例えば
圧縮空気を吹き込み、残留スラリーを完全に排出し、ガ
ス弁3が閉じ、次に排出弁2が閉じる。このサイクルを
操り返し、スラリーを連続的に排出する。
Figure 2 shows the timing of opening and closing each time, with blank spaces indicating opening and closing times.
Diagonal lines are closed. First, the introduction valve opens, and after the slurry enters, the introduction valve closes, and then the discharge valve 2 opens to discharge the slurry. During this time, the gas valve 3 is opened and compressed gas, for example compressed air, is blown in to completely discharge the residual slurry, the gas valve 3 is closed, and then the discharge valve 2 is closed. This cycle is repeated to continuously discharge the slurry.

第3図は定量容器4に冷却器5を取付けたスラリーの定
量排出装置で、定量容器の温度を下げることによって、
圧力を下げ、高圧容器からスラリーの導入を確実にする
ためのもので、スラリーの温度が高く、開閉の周期が短
い場合に有効である。
Figure 3 shows a slurry quantitative discharge device in which a cooler 5 is attached to a quantitative container 4. By lowering the temperature of the quantitative container,
This is to lower the pressure and ensure the introduction of slurry from the high-pressure container, and is effective when the temperature of the slurry is high and the opening/closing cycle is short.

第4図は定量容器4に減圧弁6を有するガス排出管16
を数句けたスラリーの定量排出装置で、定量容器内の圧
力を下げることによってスラリーの導入を完全にするも
のである。これはスラリーの排出圧が低い場合に有効で
ある。第5図はこの場合の各回の開閉時期を示したもの
で、第2図の場合の排出弁2を閉じて次に導入弁1が開
くまでの間に減圧弁の開閉を行ない、定量容器4を減圧
にして、導入弁を開きスラリーの導入を行なう。これに
よって、定量容器4の中に空隙をつくらず、スラリーを
完全に満たすことができ、排出量を正確にすることがで
きる。
FIG. 4 shows a gas discharge pipe 16 having a pressure reducing valve 6 in a metering container 4.
This is a slurry metering discharge device with several steps, which completely introduces the slurry by lowering the pressure inside the metering container. This is effective when the slurry discharge pressure is low. Figure 5 shows the timing of opening and closing each time in this case.The pressure reducing valve is opened and closed between the time when the discharge valve 2 in the case of Figure 2 is closed and the next time when the inlet valve 1 is opened. Reduce the pressure, open the introduction valve, and introduce the slurry. As a result, the metering container 4 can be completely filled with slurry without creating any voids, and the amount to be discharged can be accurate.

次に、排出量と定量容器、1サイクルの時間の関係を示
すと第1表の如くになる。
Next, Table 1 shows the relationship between the discharge amount, the quantitative container, and the time of one cycle.

−3= 表−1 この関係を式で示すと1式の様に表わされる。−3= Table-1 This relationship can be expressed as equation 1.

3600χ y=□・・・・・(1) を 但し、yは排出量(Q/hr) χは定量容器の容積(Ill) tは1サイクルの時間(sec) 以上の如く、本発明によれば、従来、困難であった、高
圧容器からの高濃度のスラリーの定量排出を確実に行な
うことが可能となり、その実用的価値は極めて大きい。
3600χ y=□...(1) where y is the discharge amount (Q/hr) χ is the volume of the quantitative container (Ill) t is the time of one cycle (sec) As described above, according to the present invention, For example, it becomes possible to reliably discharge high-concentration slurry quantitatively from a high-pressure container, which has been difficult in the past, and its practical value is extremely large.

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

第1図はスラリーの定量排出装置の実施例である。第2
図は導入弁、排出弁、ガス弁の開閉の時期を示した説明
図である。第3図は冷却器を取付−4= 、けたスラリーの定量排出装置の実施例である。第4図
は、減圧口を取付けたスラリーの定量排出装置の実施例
で、第5図は、この実施例の導入弁、排出弁、ガス弁、
減圧弁の開閉の時期を示した説明図である。 ■・・・導入弁、2・・・排出弁、3・・・ガス弁、4
・・・定量容器、5・・・冷却器、6・・・減圧弁。 第3図 第4図
FIG. 1 shows an embodiment of a slurry quantitative discharge device. Second
The figure is an explanatory diagram showing the timing of opening and closing of the introduction valve, the discharge valve, and the gas valve. FIG. 3 shows an embodiment of a quantitative discharge device for digit slurry with a cooler installed. Fig. 4 shows an embodiment of a slurry quantitative discharge device equipped with a pressure reducing port, and Fig. 5 shows the inlet valve, discharge valve, gas valve, and
It is an explanatory diagram showing timing of opening and closing of a pressure reducing valve. ■...Introduction valve, 2...Discharge valve, 3...Gas valve, 4
... Metering container, 5... Cooler, 6... Pressure reducing valve. Figure 3 Figure 4

Claims (2)

【特許請求の範囲】[Claims] (1)スラリー導入用の弁材導入管と、スラリー排出用
の回付排出管と、圧縮ガス導入用の弁材ガス導入管とを
備えた定量容器からなり、該弁材導入管と回付排出管は
それぞれ定量容器の両端部に位置していることを特徴と
するスラリーの定量排出装置。
(1) Consists of a metering container equipped with a valve material introduction pipe for slurry introduction, a recirculating discharge pipe for slurry discharge, and a valve material gas introduction pipe for introducing compressed gas, and the valve material introduction pipe and the recirculating A slurry metering discharge device characterized in that discharge pipes are located at both ends of a metering container.
(2)スラリー導入用の弁材導入管と、スラリー排出用
の回付排出管と、圧縮ガス導入用の弁材ガス導入管と、
減圧用の弁付ガス排出管とを備えた定量容器からなり、
該弁材導入管と回付排出管はそれぞれ定量容器の両端部
に位置していることを特徴とするスラリーの定量排出装
置。
(2) A valve material introduction pipe for introducing slurry, a round discharge pipe for discharging slurry, and a valve material gas introduction pipe for introducing compressed gas,
Consists of a quantitative container equipped with a gas discharge pipe with a valve for pressure reduction.
A device for quantitatively discharging slurry, characterized in that the valve material introduction pipe and the circulating discharge pipe are respectively located at both ends of a quantitative container.
JP9542283A 1983-05-30 1983-05-30 Apparatus for discharging quantitatively slurry Granted JPS59222222A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9542283A JPS59222222A (en) 1983-05-30 1983-05-30 Apparatus for discharging quantitatively slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9542283A JPS59222222A (en) 1983-05-30 1983-05-30 Apparatus for discharging quantitatively slurry

Publications (2)

Publication Number Publication Date
JPS59222222A true JPS59222222A (en) 1984-12-13
JPH0347891B2 JPH0347891B2 (en) 1991-07-22

Family

ID=14137252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9542283A Granted JPS59222222A (en) 1983-05-30 1983-05-30 Apparatus for discharging quantitatively slurry

Country Status (1)

Country Link
JP (1) JPS59222222A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2670399A1 (en) * 1990-12-14 1992-06-19 Bp Chemicals Snc METHOD AND DEVICE FOR INTRODUCING A SUSPENSION INTO A REACTOR.

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2670399A1 (en) * 1990-12-14 1992-06-19 Bp Chemicals Snc METHOD AND DEVICE FOR INTRODUCING A SUSPENSION INTO A REACTOR.
US5470540A (en) * 1990-12-14 1995-11-28 Bp Chemicals Limited Apparatus and process for introducing a suspension into a reactor

Also Published As

Publication number Publication date
JPH0347891B2 (en) 1991-07-22

Similar Documents

Publication Publication Date Title
EP0252282B1 (en) Valve for a gas container
US5238658A (en) Exhaust gas treatment apparatus
JPS59222222A (en) Apparatus for discharging quantitatively slurry
US3568833A (en) Ion exchange method and apparatus
EP0705772A2 (en) Method and device for making inert of storage enclosures
EP0293564A2 (en) Method for feeding flushing gas into a discharge hole with a slide gate nozzle for metallurgical vessels
US2838288A (en) Serpentine holding container
CN207458721U (en) A kind of power transformer oil conservater capsule air charging system
JPS57105220A (en) Oxygen-concentrating method
CN218131937U (en) Ion exchange apparatus
CN217683839U (en) Air inlet control device
CN212782421U (en) Water supply equipment experiment platform
SU1611940A1 (en) Method of charging blast furnace by cone-less charging arrangement
JPS5759026A (en) Method of cleaning turbine of supercharger
CN208752393U (en) A kind of novel developer solution liquid feeding system
DE1802417A1 (en) Device for conveying flowable material
JPS55128794A (en) Cooling water feeding system for condenser
SU750319A1 (en) Device for pneumatic transport of pulp samples
JP2771166B2 (en) Gas filling type shock absorber quick gas filling device
CN206691383U (en) Solid particulate matter discharging dust-arrest device
JPS562406A (en) Controlling device of turbine bypass valve
JPS62731B2 (en)
TW202040048A (en) Device and method for automatically emptying gas pipeline capable of achieving accelerating emptying process for the residual gas in the gas pipeline
SU1194487A1 (en) Counter-current flow sorption apparatus
JPH03110499A (en) Fuel filling device