WO1986005291A1 - Dispositif de reglage du debit d'un gaz, et application d'un tel dispositif a l'alimentation en gaz d'un reacteur - Google Patents

Dispositif de reglage du debit d'un gaz, et application d'un tel dispositif a l'alimentation en gaz d'un reacteur Download PDF

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Publication number
WO1986005291A1
WO1986005291A1 PCT/FR1986/000063 FR8600063W WO8605291A1 WO 1986005291 A1 WO1986005291 A1 WO 1986005291A1 FR 8600063 W FR8600063 W FR 8600063W WO 8605291 A1 WO8605291 A1 WO 8605291A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
capillary
flow rate
capillary tubes
tubes
Prior art date
Application number
PCT/FR1986/000063
Other languages
English (en)
French (fr)
Inventor
Guy Muller
Michel Oulie
Original Assignee
Equipements Automobiles Marchal
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 Equipements Automobiles Marchal filed Critical Equipements Automobiles Marchal
Priority to JP61501337A priority Critical patent/JPH0668360B2/ja
Priority to DE3690098A priority patent/DE3690098C2/de
Publication of WO1986005291A1 publication Critical patent/WO1986005291A1/fr

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Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/06Control of flow characterised by the use of electric means
    • G05D7/0617Control of flow characterised by the use of electric means specially adapted for fluid materials
    • G05D7/0629Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means
    • G05D7/0635Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means
    • G05D7/0641Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means
    • G05D7/0652Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means the plurality of throttling means being arranged in parallel

Definitions

  • the invention relates to a device for adjusting the flow rate of a gas from gas source dVune réelle- 'sion, upstream of the device and may move to an area downstream of the device, lower pressure this device comprising at least two capillary tubes connected in parallel between the upstream and downstream, and control means located downstream of the capillary tubes for self • riser or prevent the flow of gas in each re capillai.
  • a device of this kind is shown, for example, by FR-A-2 172493.
  • the device according to this prior document comprises a pressure reducing agent constituted by a capillary tube, by a diaphragm or by a needle valve with control manual adjustment.
  • the invention relates to such an adjustment device intended to be used with a corrosive gas, capable of forming condensates during its expansion.
  • the invention relates more particularly, but not exclusively, to a device for regulating the flow of chlorine gas used, in particular for the chlorination of scraping wiper blades of elastomeric material.
  • the object of the invention is, above all, to provide a device for adjusting the flow rate of a gas which responds better than up to now the various requirements of the practice and which, in particular, makes it possible to avoid or significantly reduce the formation of condensates, while offering possibilities for precise adjustment of the flow rate.
  • a device for adjusting the flow rate of a gas coming from a source of pressurized gas, located upstream of the device, and which can go towards a zone located downstream of the device, at lower pressure, and which comprises at least two capillary tubes mounted in parallel between the upstream and the downstream, and control means si ⁇ killed downstream of the capillary tubes to authorize or prevent the circulation of gas in each capillary is characterized by the fact that in view of its use for regulating the flow rate of a corrosive gas, capable of forming condensate during its expansion, which corresponds to a determined pressure drop (-P), the internal diameter and the length of the tubes capillaries are chosen so that the pressure gradient, i.e. the pressure drop ( ⁇ ?) distributed along the length of the tube, is sufficiently low to avoid the formation of condensates from the gas, and that capillary tubes are directly connected to the control means by conduits devoid of any other constriction member, such as a regulator.
  • the gas source is advantageously formed by a pressurized bottle containing a gas / liquid balance at the temperature considered, the bottle being maintained in a climatic chamber at a constant temperature.
  • the internal diameter and the length of the capillary tubes are chosen so that the pressure gradient is at most equal to 1 bar / mm.
  • the pressure drop ⁇ P is between 3 and 10 bars while the length of each capil ⁇ lar is at least a few millimeters and generally between 10 mm and 200 mm.
  • the control means can be formed by valves operating in completely nothing, in particular with polytetrafluoroethylene coating.
  • the capillaries generally have an internal diameter of between 0.1 mm and 0.2 mm.
  • capillary tubes and the conduits are made of a material that is inert with respect to the corrosive gas.
  • the capillary tubes can be made of glass, while the - conduits are made of polytetrafluoroethylene.
  • the capillary tubes are chosen so as to each determine a flow rate different from that of the other capillaries, the capillary tube of higher rank having in particular a flow twice that of the capillary of immediately lower rank.
  • the device may include four capillaries arranged in parallel, the capillary of rank or lower weight ensuring a flow rate of 0.0625 1 / min, while the following capillaries respectively provide flow rates of 0.125 1 / min, 0.25 1 / min, 0.5 1 / min.
  • a particularly advantageous application of such a flow control device relates to the supply of a reactor for fixing a gas to a solid, in particular for the chlorination of wiper blades of elastomeric material. .
  • a reactor and the corresponding treatment process have been described in.
  • electromagnetic valves are avar.tagement to authorize or prevent the circulation of gas in each capillary, the control of these solenoid valves being controlled by various parameters such as the speed of movement of the solid to be treated, the temperature ⁇ treatment size, the temperature of the gas source, etc.
  • the invention consists, apart from the provisions set out above, in a certain number of other provisions which will be more explicitly discussed below, with regard to a particular embodiment described with reference to the attached drawing, but which is by no means limiting.
  • Figure 1 of this drawing is a diagram of an adjustment device according to the invention.
  • Figure 2 is a diagram of an application of such a device to the supply of a reactor for fixing a gas on a solid.
  • a device D for adjusting the flow rate of a gas namely chlorine in the example considered, coming from a source of pressurized gas 1, located at upstream of the device D.
  • the gas source is formed by a cylinder 2, under pressure, containing a gas / liquid balance at the temperature considered. This temperature is therefore lower than the critical temperature of the gas.
  • the bottle 2 is advantageously kept in a climatic chamber E, at constant temperature, in particular at a temperature of 13C C for which the equilibrium pressure gas / liq ide was 5.5 bar absolute and therefore 4.5 relative bars.
  • the gas can go, in the direction of the arrows F, to a zone A, located downstream of the device D, being at a pressure lower than the pressure of the gas in the source 1.
  • the device D is located a temperature also lower than the critical temperatures of the gas under consideration, chlorine in the example envisaged, and of the vapors, in turn water vapor, conveyed by this gas.
  • the gas is liable to form condensates when it relaxes from the upstream pressure which prevails in the source 1, to the downstream pressure which prevails in zone A.
  • the device D comprises several capillary tubes; es C1, C2, C3, C4, mounted in parallel between upstream and downstream. '> In the example shown, four capillary tubes C1-C4 are provided ; it is clear that a different number of capillary tubes can be used as required.
  • the capillary tubes C1-C4 are mounted in conduits _t1, t2, t3, t.4, connected in parallel to an inlet pipe 3, transverse, itself connected by a pipe 4 to the source 1. At their other end, the conduits t1-t_4 are connected in parallel to another transverse tube 5, itself connected by a pipe 6 to the zone A of gas use.
  • the capillary tubes C1-C4 are preferably made of glass, while the conduits t -.4 can be made of poly ⁇ tetrafluoroethylene.
  • the internal diameter and the length of the C1-C4 capillary tubes are chosen so that the pressure gradient, created by each capillary tube, is sufficiently small to avoid the formation of condensates from the gas.
  • Sil_ denotes the length of a capillary, for chlorine, the pressure gradient AP / l is at most equal to 1 bar / mm and preferably less than 0.5 bar / mrn.
  • the capillaries available on the market generally have an internal diameter which can vary from 0.1 mm to 0.2 mm with an intermediate diameter of 0.15 mm.
  • the length of the capillaries C1-C4 is several millimeters. This length can vary in particular from 10 mm to 200 mm for an ⁇ P of 3 to 10 bars, for chlorine.
  • Control means B are further provided for authorizing or preventing the circulation of gas in each capil C1-C4, and therefore in the corresponding conduit Jt1-_t4.
  • These control means B are advantageously formed by valves y_1-y_4 associated with each conduit t -_t4.
  • These valves v1-_4 are of the all-or-nothing type, that is to say that they are either fully open or completely closed.
  • These v1-v4 valves can be manual, or, preferably, electromagnetically controlled (electro ⁇ valves), in particular with polytetrafluoroethylene coating.
  • the valves y_1-y_4 are arranged downstream of the capillary tubes on each conduit _t1- 4. No throttling member is placed between the capillaries C1-C4 and the valves _y_1-v.
  • the flow rates of each capillary C1-C4 are different.
  • the flow rates are chosen so that, if the capillaries are classified in ascending order of their flow rate, the capillary of higher rank has a flow rate twice that of the capillary of immediately lower rank.
  • the capillary C4 will be the minimum flow capillary, while the capillaries C3, C2 will have progressively increasing flow rates.
  • the capillary C3 assu ⁇ rera a flow twice that of the capillary C4; the capillary i "e C2 will ensure a flow rate double that of C3, and likewise for C1, with respect to C2.
  • the maximum desired chlorine flow rate is of the order of 1 1 / min.
  • a flow rate of 0.0625 1 / min is chosen.
  • the capillaries C3, C2, C1 will, respectively, have flow rates of 0.125 1 / min; 0.25 1 / min; and 0.5 1 / min.
  • the different flow rates that can be obtained are separated by a quantum of 0.0625 1 / min.
  • FIG. 2 illustrates, in summary, the application of such a device to the supply of a reactor 7, diagrammatically shown, for the chlorination of wiper blades, made of elastomeric material, traveling in the form of 'a continuous ribbon 8.
  • the reactor 7, as described in patent FR 2 537 014 already cited, consists for example of a tube slightly inclined relative to the vertical, provided at its upper part with a suitable sealing device ⁇ required 9 allowing the passage of the ribbon 8. At its lower part, the tube 7 plunges into a tank 10 containing liquid, in particular water, to form a liquid seal.
  • the reaction gas chlorine in the example envisaged
  • the reaction gas is introduced into the lower part of the reactor 7 by a tube 11.
  • the ribbon 8 the surface of which has been treated in the reactor 7 by reaction with chlorine, leaves the reactor 7 by plunging into the tank 10 and then emerging from this tank.
  • the electromagnetic valves _1-y_4 of the device D for adjusting the flow rate are advantageously controlled from a computer 12 which receives information on various operating parameters such as the speed of travel of the ribbon 8 , supplied by a sensor 13, the temperature inside the reactor 7 supplied by a temperature measurement probe 14. It can be the same for any parameter that one wishes to take into consideration. From the information provided by the various sensors and probes, the computer 12 determines, by example from a pre-established program or law, the required chlorine flow rate and therefore controls the closing or opening of each of the valves y_1-_4.

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  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Pipeline Systems (AREA)
  • Flow Control (AREA)
PCT/FR1986/000063 1985-03-01 1986-02-26 Dispositif de reglage du debit d'un gaz, et application d'un tel dispositif a l'alimentation en gaz d'un reacteur WO1986005291A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61501337A JPH0668360B2 (ja) 1985-03-01 1986-02-26 ガスの流量を調整する装置と反応器へのガスの供給に対するこのような装置の応用
DE3690098A DE3690098C2 (de) 1985-03-01 1986-02-26 Vorrichtung zum Einstellen der Durchflußmenge eines Gases

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8503034A FR2578336B1 (fr) 1985-03-01 1985-03-01 Dispositif de reglage du debit d'un gaz, et application d'un tel dispositif a l'alimentation en gaz d'un reacteur
FR85/03034 1985-03-01

Publications (1)

Publication Number Publication Date
WO1986005291A1 true WO1986005291A1 (fr) 1986-09-12

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ID=9316777

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FR1986/000063 WO1986005291A1 (fr) 1985-03-01 1986-02-26 Dispositif de reglage du debit d'un gaz, et application d'un tel dispositif a l'alimentation en gaz d'un reacteur

Country Status (5)

Country Link
JP (1) JPH0668360B2 (enrdf_load_stackoverflow)
DE (2) DE3690098C2 (enrdf_load_stackoverflow)
FR (1) FR2578336B1 (enrdf_load_stackoverflow)
SU (1) SU1482539A3 (enrdf_load_stackoverflow)
WO (1) WO1986005291A1 (enrdf_load_stackoverflow)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2674213A1 (en) * 2012-06-14 2013-12-18 Basell Polyolefine GmbH Method for cooling a gas-phase reactor for the polymerization of olefins
WO2013186299A1 (en) * 2012-06-14 2013-12-19 Basell Polyolefine Gmbh Method for cooling a gas-phase reactor for the polymerization of olefins

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2424184A (en) * 2005-03-14 2006-09-20 Kidde Ip Holdings Ltd Inert gas fire suppression system
CN113769594A (zh) * 2021-09-06 2021-12-10 苏州晟宇气体设备有限公司 标准气体多元混合系统

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2172493A5 (enrdf_load_stackoverflow) * 1972-02-15 1973-09-28 Oxhydrique Francaise
US4030523A (en) * 1976-04-19 1977-06-21 The United States Of America As Represented By The Secretary Of The Navy Digital flow control system
GB2049225A (en) * 1979-04-06 1980-12-17 Boc Ltd Fluid-flow restricting apparatus for mixing fluids
FR2537014A1 (fr) * 1982-12-06 1984-06-08 Marchal Equip Auto Reacteur pour la fixation d'un gaz sur un solide, utilisable notamment pour la chloration de lames racleuses d'essuie-glaces

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0017408A1 (en) * 1979-04-06 1980-10-15 BOC Limited Apparatus for mixing fluids comprising fluid-flow restricting device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2172493A5 (enrdf_load_stackoverflow) * 1972-02-15 1973-09-28 Oxhydrique Francaise
US4030523A (en) * 1976-04-19 1977-06-21 The United States Of America As Represented By The Secretary Of The Navy Digital flow control system
GB2049225A (en) * 1979-04-06 1980-12-17 Boc Ltd Fluid-flow restricting apparatus for mixing fluids
FR2537014A1 (fr) * 1982-12-06 1984-06-08 Marchal Equip Auto Reacteur pour la fixation d'un gaz sur un solide, utilisable notamment pour la chloration de lames racleuses d'essuie-glaces

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2674213A1 (en) * 2012-06-14 2013-12-18 Basell Polyolefine GmbH Method for cooling a gas-phase reactor for the polymerization of olefins
WO2013186299A1 (en) * 2012-06-14 2013-12-19 Basell Polyolefine Gmbh Method for cooling a gas-phase reactor for the polymerization of olefins
US9694336B2 (en) 2012-06-14 2017-07-04 Basell Polyolefine Gmbh Method for cooling a gas-phase reactor for the polymerization of olefins

Also Published As

Publication number Publication date
DE3690098C2 (de) 1995-06-01
SU1482539A3 (ru) 1989-05-23
JPH0668360B2 (ja) 1994-08-31
FR2578336A1 (fr) 1986-09-05
FR2578336B1 (fr) 1988-07-08
JPS62501986A (ja) 1987-08-06
DE3690098T (enrdf_load_stackoverflow) 1987-06-04

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