JPS5973044A - Automatic pressure adjusting type small reaction apparatus - Google Patents

Automatic pressure adjusting type small reaction apparatus

Info

Publication number
JPS5973044A
JPS5973044A JP18374882A JP18374882A JPS5973044A JP S5973044 A JPS5973044 A JP S5973044A JP 18374882 A JP18374882 A JP 18374882A JP 18374882 A JP18374882 A JP 18374882A JP S5973044 A JPS5973044 A JP S5973044A
Authority
JP
Japan
Prior art keywords
pressure
automatic
valve
control valve
supply line
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
JP18374882A
Other languages
Japanese (ja)
Other versions
JPH0210688B2 (en
Inventor
Junji Honma
淳司 本間
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.)
HONMA RIKEN KOGYO KK
Original Assignee
HONMA RIKEN KOGYO KK
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 HONMA RIKEN KOGYO KK filed Critical HONMA RIKEN KOGYO KK
Priority to JP18374882A priority Critical patent/JPS5973044A/en
Priority to DE19833336750 priority patent/DE3336750A1/en
Priority to US06/540,670 priority patent/US4556537A/en
Priority to GB08327647A priority patent/GB2129703B/en
Priority to FR838316481A priority patent/FR2534489B1/en
Publication of JPS5973044A publication Critical patent/JPS5973044A/en
Publication of JPH0210688B2 publication Critical patent/JPH0210688B2/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
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0005Catalytic processes under superatmospheric pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE:To keep the supply amount of a stock material constant, by automatically and rapidly controlling an automatic back pressure valve, a control valve and automatic pressure control valve respectively. CONSTITUTION:An automatic pressure control valve 1 is provided to a stock material supply line 6 and a flow meter 2 having a control valve 7 is provided to the stock material supply line 6 at the downstream side of the automatic pressure control valve 1. A pressure controlling automatic adjusting mechanism 8 for measuring the pressure of the stock material supply line 6 between the automatic pressure control valve 1 and the flow meter 2 to generate a signal corresponding to the difference with set pressure to control the automatic pressure control valve 1 is provided while a flow amount controlling automatic adjusting mechanism 9 for measuring the flow amount of the flow meter 2 to generate the signal corresponding to the difference with a set flow amount to contol the valve 7 is mounted. To a product withdrawing line 11, a back pressure controlling automatic adjusting mechanism 10 for measuring pressures of an automatic back pressure valve 5 and the stock material supply line 6 to generate the signal corresponding to set pressure is mounted.

Description

【発明の詳細な説明】 本発明は自動圧力調節小型反応装置に関し、詳しくは反
応部分の容積が非常に小さく、かつ反応圧力の非常に高
い化学実験等に好適に使用しうる反応装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a small-sized reaction apparatus with automatic pressure control, and more particularly to a reaction apparatus which has a very small volume of reaction part and can be suitably used for chemical experiments and the like where the reaction pressure is very high.

従来から小型で高圧の反応装置は種々のものが知られて
いる。そのうち現在使用されている最も小型のものは、
反応温度の調節および原料供給速度の調節は自動的に行
なうが、反応圧力の調節は手動によシ行なうタイプのも
のである。一般に、圧力の調節は、ダイヤフラム型の調
節弁で行なわれることが多い。しかし、このようなタイ
プのものは調節に際しての応答が遅いため、小型の反応
装置に設置すると圧力変動が大きく実用に適しないもの
である。
Various types of small-sized, high-pressure reactors have been known. The smallest one currently in use is
Although the reaction temperature and raw material supply rate are automatically controlled, the reaction pressure is manually controlled. Generally, pressure is often adjusted using a diaphragm type control valve. However, this type of reactor has a slow response during adjustment, and when installed in a small reactor, pressure fluctuations are large, making it unsuitable for practical use.

本発明は上記の間顕点を解消し、応答が速く圧力調節を
高い精度で行なうことのできる小型の反応装置を提供す
ることを目的とするものである。
It is an object of the present invention to provide a small-sized reaction apparatus which eliminates the above-mentioned problem and can respond quickly and adjust pressure with high accuracy.

本発明の装置を第1図に基いて説明すれば1本発明は、
原料供給ライン6に設けた自動調圧弁1゜該自動調圧弁
1の下流側の原料供給ライン乙に設けた調節弁7を有す
る流量計2.前記自動調圧弁1と流量計2の間の原料供
給ライン乙の圧力を測定して設定圧との差に応じた信号
を発生せしめて自動調圧弁1を制御する調圧用自動調整
機構8゜前記流量計2の流量を測定して設定流量との差
に応じた信号を発生せしめて調節弁7を制御する流量調
節用自動調整機構9.前記原料供給ライン6を入口側に
接続しかつ生成物抜出しライン11を出口側に接続した
流通式の小型反応器6.前記生成物抜出しライン11に
設けた自動背圧弁5および前記調節弁7の下流側の原料
供給ライン6の圧力を測定して設定圧との差に応じた信
号を発生せしめて自動背圧弁5を制御する背圧調節用自
動調整機構10よシなる自動圧力調節小型反応装置であ
る。
The device of the present invention will be explained based on FIG. 1.
Automatic pressure regulating valve 1° provided in the raw material supply line 6; Flowmeter 2 having a regulating valve 7 provided in the raw material supply line B on the downstream side of the automatic pressure regulating valve 1. An automatic pressure adjustment mechanism 8° for controlling the automatic pressure adjustment valve 1 by measuring the pressure in the raw material supply line B between the automatic pressure adjustment valve 1 and the flow meter 2 and generating a signal according to the difference from the set pressure. 9. An automatic adjustment mechanism for flow rate adjustment that measures the flow rate of the flow meter 2 and generates a signal according to the difference from the set flow rate to control the control valve 7. 6. A small flow reactor in which the raw material supply line 6 is connected to the inlet side and the product extraction line 11 is connected to the outlet side. The automatic back pressure valve 5 is activated by measuring the pressure in the raw material supply line 6 on the downstream side of the automatic back pressure valve 5 provided in the product extraction line 11 and the control valve 7, and generating a signal according to the difference from the set pressure. This is an automatic pressure regulating small reaction device including an automatic regulating mechanism 10 for controlling back pressure.

上記のような構成よりなる本発明の反応装置によれば、
小型反応器5内の反応圧を速やかにかつ高精度にて自制
調節することができ、特に原料供給量が少ない微少流鳳
系での小型反応器内の圧力調節を正確にしかも自動的に
行なうことができる。
According to the reaction apparatus of the present invention having the above configuration,
The reaction pressure inside the small reactor 5 can be self-controlled and adjusted quickly and with high precision, and the pressure inside the small reactor can be adjusted accurately and automatically, especially in a micro flow system where the amount of raw material supplied is small. be able to.

本発明の反応装置を用いて小型反応器5内の圧力調節を
行なう手順の一例を説明すれば次のとおシである。まず
自動調圧弁1と流量計2の間の原料供給ライン乙の圧力
P、と、流量計2に付設している調節弁7の下流側の連
判供給ライン6の圧力P2との差、即ちP、 −P、が
好適圧力差(例えば2 Wcrl程度)に維持されるよ
うに自動調圧弁1を開く。
An example of the procedure for adjusting the pressure inside the small reactor 5 using the reaction apparatus of the present invention is as follows. First, the difference between the pressure P in the raw material supply line B between the automatic pressure regulating valve 1 and the flow meter 2 and the pressure P2 in the continuous supply line 6 on the downstream side of the regulating valve 7 attached to the flow meter 2, that is, P , -P, is maintained at a suitable pressure difference (for example, about 2 Wcrl), the automatic pressure regulating valve 1 is opened.

ここで好適圧力差とは流量計の性能を発揮させるのに最
も好ましい圧力差であり、PlとP2の圧力差が大きす
ぎると流量調節弁7にかかる負荷が大きくなシすぎて適
正な調節ができなくなり、逆に圧力差が小さすぎると原
料の流れが円滑に進行しなくなる。この場合の調節は、
圧力P1を圧力センサー等にて検知し、これを電圧ある
いは電流に変換した情報として電子計算機等に入力し、
ここで設定圧力と人力した圧力P1を比較してその圧力
差に応じた信号(パルスなど)を発生させ、この借上で
自動調圧弁1の駆動機構(例えばステップモーターなど
)を動かすことによって行なう。なお圧力センサー、電
子計算機、信号発生機(例えばパルス送信機)等を組合
せて、圧力検知から演算処理、さらに信号発生に至るま
での一連の処理を行なう機構を、本明細書では自動調整
機構と総称する。
The suitable pressure difference here is the most preferable pressure difference for the performance of the flowmeter to be exhibited. If the pressure difference between Pl and P2 is too large, the load on the flow control valve 7 will be too large and proper adjustment will not be possible. On the other hand, if the pressure difference is too small, the raw material will not flow smoothly. In this case, the adjustment is
Detect the pressure P1 with a pressure sensor, etc., convert it into voltage or current, and input it into a computer, etc.
Here, the set pressure and the manually applied pressure P1 are compared, a signal (such as a pulse) is generated according to the pressure difference, and this signal is used to move the drive mechanism (for example, a step motor) of the automatic pressure regulating valve 1. . In this specification, a mechanism that combines a pressure sensor, an electronic computer, a signal generator (for example, a pulse transmitter), etc., and performs a series of processes from pressure detection to calculation processing and signal generation is referred to as an automatic adjustment mechanism. collectively.

従って本発明では、調圧用自動調整機構8にて自動調圧
弁1を制御し、圧力P、を調節することとなる。
Therefore, in the present invention, the automatic pressure regulating valve 1 is controlled by the automatic pressure regulating mechanism 8 to regulate the pressure P.

一方1原料供給ライン6から小型反応器5へ導入する原
料の供給量は、流量計2からの情報を流量調節用自動調
整機構9に入力して、ここで演算を行なうと共に調節弁
7へ信号を発信して、該調節弁7を開閉することKより
所定息に調節、される。
On the other hand, the amount of raw material introduced from the first raw material supply line 6 to the small reactor 5 is determined by inputting the information from the flow meter 2 to the automatic flow rate adjustment mechanism 9, which performs calculations and sends a signal to the control valve 7. The breath is regulated to a predetermined value by transmitting K and opening and closing the control valve 7.

このような状況において、小型反応器6内の圧力を高め
るには、前記圧力P2の値を電流あるいは電圧に変換し
て背圧調節用自動調整機構1oに入力し、これを予め設
定しである圧力と比較してその圧力差に応じた信号を発
生せしめて、この信号により自動背圧弁5の駆動機構を
動がして該背圧弁5を絞る。ここで信号を発生するにあ
たっては、設定圧と測定圧烏との差に比例した強度の信
号(パルスの数あるいは強度、電流級、電圧、空気圧な
ど)を一度に生ぜしめて、自動背圧弁5を絞ってもよい
が、設定圧と測定圧P、との差がある限り、その差の大
きさによらず一定の強度の信号を発生させ、自動背圧弁
5を一定角度だけ回して絞り、これを数回繰返して徐々
に自動背圧弁5を絞って昇圧する方が好ましい。この場
合、圧力P、の測定から信号発生、自動背圧弁5の作動
の一連の自動操作は一定時間、例えば2〜4秒ごとに進
行するようセットすることが好ましく、また−回の操作
でα01〜11J/c!Iの範囲で昇圧するように自動
背圧弁5を動かす駆動機構(ステップモーターなど)を
調整しておくことが好ましい。なおこのような操作に適
した自動背圧弁としては第2図に示すようなものをあげ
ることができる。
In such a situation, in order to increase the pressure inside the small reactor 6, the value of the pressure P2 is converted into current or voltage, inputted to the back pressure adjustment automatic adjustment mechanism 1o, and set in advance. A signal corresponding to the pressure difference is generated by comparing the pressure, and the drive mechanism of the automatic back pressure valve 5 is actuated by this signal to throttle the back pressure valve 5. To generate the signal here, a signal (number or intensity of pulses, current class, voltage, air pressure, etc.) with an intensity proportional to the difference between the set pressure and the measured pressure is generated at once, and the automatic back pressure valve 5 is activated. However, as long as there is a difference between the set pressure and the measured pressure P, a signal with a constant intensity is generated regardless of the size of the difference, and the automatic back pressure valve 5 is turned by a certain angle to throttle it. It is preferable to repeat this several times and gradually throttle the automatic back pressure valve 5 to increase the pressure. In this case, it is preferable to set the series of automatic operations from measuring the pressure P, generating a signal, and operating the automatic back pressure valve 5 to proceed at a fixed time interval, for example, every 2 to 4 seconds. ~11J/c! It is preferable to adjust the drive mechanism (such as a step motor) that operates the automatic back pressure valve 5 so that the pressure is increased within the range of I. An example of an automatic back pressure valve suitable for such an operation is the one shown in FIG.

上述の如く、自動背圧弁5を絞ると圧力P、け上昇する
が、同時に原料供給ライン6の流量は減少する傾向を示
す。しかしこの流量の減少は流肘計2から直ちに流量調
節用自動調整機構9に入力され、ここで設定流量との差
に応じて調節弁7へ信号が送られ、この信号によって調
節弁7が緩められて流量が増え、もとの流量に速やかに
回復する。
As described above, when the automatic back pressure valve 5 is throttled, the pressure P increases, but at the same time, the flow rate of the raw material supply line 6 tends to decrease. However, this decrease in flow rate is immediately input from the flow meter 2 to the automatic flow rate adjustment mechanism 9, which sends a signal to the control valve 7 according to the difference from the set flow rate, and this signal causes the control valve 7 to loosen. The flow rate increases and quickly returns to the original flow rate.

次に、調節弁7の開度が大きくなると、前述した圧力P
1とP2との差が小さくなシ、これは圧力P。
Next, when the opening degree of the control valve 7 increases, the above-mentioned pressure P
If the difference between 1 and P2 is small, this is pressure P.

の低下となって現われる。しかし本発明では、この圧力
P1の低下の情報は直ちに調圧用自動調整機構8へ入力
され、ここで設定圧力との差に応じて自動調圧弁1へ信
号が送られ、この信号によって自動調圧弁1が緩められ
て圧力P1が上昇することとなる。
This appears as a decrease in However, in the present invention, information on the decrease in pressure P1 is immediately input to the automatic pressure regulating mechanism 8, which sends a signal to the automatic pressure regulating valve 1 according to the difference from the set pressure, and this signal causes the automatic pressure regulating valve to 1 is loosened, and the pressure P1 increases.

このように自動背圧弁5.調節弁7.自動調圧弁1の各
々を自動的にかつ速やかに調節することによって、反応
器6へ供給する原料の供給量を一定に保持しつつ、反応
器3の圧力を所望する高圧下洗まで速やかに昇圧するこ
とができる。
Thus automatic back pressure valve 5. Control valve7. By automatically and quickly adjusting each of the automatic pressure regulating valves 1, the pressure of the reactor 3 can be quickly increased to the desired high-pressure underwashing while keeping the amount of raw material supplied to the reactor 6 constant. can do.

斜上の如く本発明の装置によれば、超小型の反応器を用
いる微少流量系での圧力の調節を速やかにかつ高い精度
でしかも自動的に行なうことができる。したがって本発
明の装置は、小型でしかも正確な条件設定の要求される
化学実験などに用いる装置として好適に利用される。
According to the apparatus of the present invention, such as the one shown on the top, it is possible to quickly and automatically adjust the pressure in a minute flow rate system using an ultra-small reactor. Therefore, the apparatus of the present invention is suitably used as an apparatus for use in chemical experiments, etc., which require small size and accurate setting of conditions.

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

第1図は本発明の装置の一例を示す説明図、第2図は本
発明の装置に使用する自動背圧弁の御粘様を示す断面概
略図である。 1・・・自動調圧弁、2・・・流量計、6・・・小型反
応器。 4・・・加熱帯、5・・・自動背圧弁、6・・・原料供
給ライン、7・・・調節弁、8・・・調圧用自動調整機
構。 9・・・流量調節用自動調整機構、10・・・背圧調節
用自動調整機構、11・・・生成物抜出しライン。 12・・・原料供給部、  15.14・・・圧力セン
サー。 15・・・駆動機構、16・・・減速ギヤ、17・・ス
プリング、18・・・主バルブ。 特許出願人  本間理研工業有限会社 ]1 251
FIG. 1 is an explanatory view showing an example of the device of the present invention, and FIG. 2 is a schematic cross-sectional view showing the appearance of an automatic back pressure valve used in the device of the present invention. 1... Automatic pressure regulating valve, 2... Flow meter, 6... Small reactor. 4... Heating zone, 5... Automatic back pressure valve, 6... Raw material supply line, 7... Control valve, 8... Automatic adjustment mechanism for pressure regulation. 9...Automatic adjustment mechanism for flow rate adjustment, 10...Automatic adjustment mechanism for back pressure adjustment, 11...Product extraction line. 12... Raw material supply section, 15.14... Pressure sensor. 15... Drive mechanism, 16... Reduction gear, 17... Spring, 18... Main valve. Patent applicant Honma Riken Kogyo Co., Ltd.] 1 251

Claims (1)

【特許請求の範囲】[Claims] (1)  原料供給ライン(6)に設けた自動調圧弁(
1)。 該自動調圧弁(1)の下流側の原料供給ライン(6)に
設けた調節弁(7)を有する流量計(2)、前記自動調
圧弁(1)と流量計(2)の間の原料供給ライン(6)
の圧力を測定して設定圧との差により信号を発生せしめ
て自動調圧弁(1)を制御する調圧用自動調整機構(8
)、前記流量計(2)の流量を測定して設定流量との差
により信号を発生せしめて調節弁(7)を制御する流鰍
調節用自動調整機構(9)、前記原料供給ライン(6)
を入口側に接続しかつ生成物抜出しライン(11)を出
口側に接続した流通式の小型反応器(3)、前記生成物
抜出しライン(11)に設けた自動背圧弁(5)および
前記調節弁(7)の下流側の原料供給ライン(6)の圧
力を測定して設定圧との差により信号を発生せしめて自
動背圧弁(5)を制御する背圧調節用自動調整機構(1
0)よりなる自動圧力調節小型反応装置。
(1) Automatic pressure regulating valve (
1). A flow meter (2) having a regulating valve (7) provided in a raw material supply line (6) downstream of the automatic pressure regulating valve (1), and a raw material between the automatic pressure regulating valve (1) and the flow meter (2). Supply line (6)
An automatic pressure adjustment mechanism (8) that measures the pressure of
), an automatic adjustment mechanism (9) for controlling the control valve (7) by measuring the flow rate of the flowmeter (2) and generating a signal based on the difference from the set flow rate to control the control valve (7); and the raw material supply line (6). )
a small flow reactor (3) connected to the inlet side and a product withdrawal line (11) connected to the outlet side, an automatic back pressure valve (5) provided in the product withdrawal line (11), and the adjustment An automatic back pressure adjustment mechanism (1) that measures the pressure in the raw material supply line (6) downstream of the valve (7) and generates a signal based on the difference from the set pressure to control the automatic back pressure valve (5).
0) Automatic pressure regulating small reactor.
JP18374882A 1982-10-15 1982-10-21 Automatic pressure adjusting type small reaction apparatus Granted JPS5973044A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP18374882A JPS5973044A (en) 1982-10-21 1982-10-21 Automatic pressure adjusting type small reaction apparatus
DE19833336750 DE3336750A1 (en) 1982-10-15 1983-10-08 REACTOR
US06/540,670 US4556537A (en) 1982-10-15 1983-10-11 Reactor
GB08327647A GB2129703B (en) 1982-10-15 1983-10-14 Reactor
FR838316481A FR2534489B1 (en) 1982-10-15 1983-10-17 REACTOR FOR USE, ESPECIALLY IN CHEMICAL EXPERIENCES

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18374882A JPS5973044A (en) 1982-10-21 1982-10-21 Automatic pressure adjusting type small reaction apparatus

Publications (2)

Publication Number Publication Date
JPS5973044A true JPS5973044A (en) 1984-04-25
JPH0210688B2 JPH0210688B2 (en) 1990-03-09

Family

ID=16141283

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18374882A Granted JPS5973044A (en) 1982-10-15 1982-10-21 Automatic pressure adjusting type small reaction apparatus

Country Status (1)

Country Link
JP (1) JPS5973044A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0361844A (en) * 1989-07-31 1991-03-18 Idemitsu Kosan Co Ltd Measuring apparatus for reaction of gas when temperature is increased

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0361844A (en) * 1989-07-31 1991-03-18 Idemitsu Kosan Co Ltd Measuring apparatus for reaction of gas when temperature is increased

Also Published As

Publication number Publication date
JPH0210688B2 (en) 1990-03-09

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