GB2204363A - Metering liquid or thick substances - Google Patents

Metering liquid or thick substances Download PDF

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Publication number
GB2204363A
GB2204363A GB08809110A GB8809110A GB2204363A GB 2204363 A GB2204363 A GB 2204363A GB 08809110 A GB08809110 A GB 08809110A GB 8809110 A GB8809110 A GB 8809110A GB 2204363 A GB2204363 A GB 2204363A
Authority
GB
United Kingdom
Prior art keywords
tank
intermediate storage
substances
weight
valve
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.)
Withdrawn
Application number
GB08809110A
Other versions
GB8809110D0 (en
Inventor
Jean-Marie Chauveau
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.)
HASLER FRERES INTERNATIONAL SA
Original Assignee
HASLER FRERES INTERNATIONAL SA
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 HASLER FRERES INTERNATIONAL SA filed Critical HASLER FRERES INTERNATIONAL SA
Publication of GB8809110D0 publication Critical patent/GB8809110D0/en
Publication of GB2204363A publication Critical patent/GB2204363A/en
Withdrawn legal-status Critical Current

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Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F11/00Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
    • G01F11/28Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with stationary measuring chambers having constant volume during measurement
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01GWEIGHING
    • G01G13/00Weighing apparatus with automatic feed or discharge for weighing-out batches of material
    • G01G13/24Weighing mechanism control arrangements for automatic feed or discharge
    • G01G13/242Twin weighing apparatus; weighing apparatus using single load carrier and a plurality of weigh pans coupled alternately with the load carrier; weighing apparatus with two or more alternatively used weighing devices
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01GWEIGHING
    • G01G13/00Weighing apparatus with automatic feed or discharge for weighing-out batches of material
    • G01G13/24Weighing mechanism control arrangements for automatic feed or discharge
    • G01G13/26Weighing mechanism control arrangements for automatic feed or discharge involving fluid-pressure systems
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01GWEIGHING
    • G01G17/00Apparatus for or methods of weighing material of special form or property
    • G01G17/04Apparatus for or methods of weighing material of special form or property for weighing fluids, e.g. gases, pastes
    • G01G17/06Apparatus for or methods of weighing material of special form or property for weighing fluids, e.g. gases, pastes having means for controlling the supply or discharge

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  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Basic Packing Technique (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

2 2 0 4 3 6 J.31 PROCESS FOR METERING LIQUID OR THICK SUBSTANCES AND
INSTALLATION FOR CARRYING OUT THIS PROCESS This invention relates to a process for metering liquid or thick substances.
It also relates to an installation for metering liquid or thick substances enabling the above process to be carried out and having a supply vat containing the substances to be metered, means for tapping predeterm ined masses or volumes of these substances and means for discharging said predetermined masses or volumes in a controlled way.
Traditionally pumps are used for regulating the flow of liquids to be metered. The use of a tank supported by a weighing machine enables the weight of liquids to be metered to be regulated and thus the duty of the pump to be associated with the desired loss in weight per unit of time. Such appliances are known by the name of regulateddrainage hoppers or differential gravimetric flow control devices.
In these installations, pumps are weak components which may leak, which are likely to pollute the metered liquid and which in all cases require a lot of maintenance.
Moreover, viscous or thick substances generally cannot be metered in installations of this type.
The object of this invention is to remove the above drawbacks by developing a process and perfecting an in stallation for metering liqiid or thick substances with out a pump.
To this end, the process according to the invention is characterised in that predetermined masses or volumes of substances to be metered are tapped, in that these predetermined masses or volumes are temporarily stored 2 in at least one intermediate storage tank of known weight and/or volume, in that these predetermined masses or volumes are subjected to the pressure of a gas and in that the opening of a,relief valve and/or the press ure of said gas in said tank is regulated so that the flow of said predetermined masses or volumes occurs within a given time.
According to a preferred embodiment, two intermediate storage tanks arranged in parallel are used and one of these intermediate storage tanks is filled during at most a part of the time required to empty the other.
Means for filling and emptying intermediate storage tanks are preferably designed so that one of these tanks can be filled within a period of time less than the minimum time required to empty the other tank.
The weight of predetermined masses of substances con tained in the intermediate storage tanks is preferably determined by weighing said tanks.
During the emptying of the tank, the variation in weight of the tank containing the substances to be metered is preferably regulated continuously and the discharge flow of these substances is regulated by adjusting the pressure of the gas injected into the tank and/or the opening of the relief valve.
According to an advantageous embodiment, metering is carried out as follows:
- the supply valve of the previously filled intermediate tank is closed, the escape valve of this tank is opened, - the tank is pressurised, - a chain for measuring the weight of the two tanks is activated, 3 the relief valve of the filled tank is progress ively opened and the relief valve of the emptied tank is progressively closed, the chain for measuring the weight of the filled tank is activated, - the inlet o. f the pressurised gas into the empty tank is closed, the supply valve of the empty tank is opened, the weight of this tank is regulated as it is filled so as to ascertain the moment when it is regarded as being full, and the corresponding supply valve is closed.
The installation according to the invention is character- ised in that the means for tapping said predetermined masses or volumes and the means for discharging them comprise at least one intermediate storage_tank, a pressurised gas generating device for subjecting the substances contained in this tank to the pressure of this gas, at least one relief and/or control valve mounted on a drainage line of this tank and elements for reg ulating and controlling the pressurised gas generating device and the opening of the relief and/or control valve.
According to a first preferred. embodiment of this installation, it comprises two intermediate storage tanks connected in parallel to the supply vat and a dis charge circuit comprising two relief and control valves respectively connected to each of the two tanks.
According to a second preferred embodiment, it comprises two intermediate storage tanks connected in parallel to the supply vat and a discharge circuit comprising two relief valves respectively connected to each of the two tanks and a single control valve.
4 Each intermediate storage tank is advantageously conn ected to a weighing machine designed to measure the weight of this tank containing a predetermined mass of substance to be metered. The control valve is preferably of the type having a pneumatic 0-ring.
The present invention and its various advantages will be better understood by reference to the description of a preferred exemplified embodiment and of the attached drawing in which the single figure represents the install ation according to the invention in diagrammatic form.
With reference to the figure, the installation described comprises a supply vat 10 containing a liquid or thick substance 11 to be metered, two intermediate storage tanks 12 and 13 connected in parallel by means of lines 14 and 15 to supply vat 10 and two discharge lines 16 and 17 connected between them and to an outlet line 18.
Supply valves 20 and 21 are respectively mounted on supply lines 14 and 15 and relief and/or control valves 22 and 23 are respectively mounted on discharge lines 16 and 17.
An air compressor 24, which could be replaced by var ious other pressurised gas sources, is connected to a pressure distributor 25 itself coupled to the two inter mediate storage tanks 12 and 13. Each of these tanks is connected to a weighing machine 26 and 27 respect ively. Moreover, intermediate storage tank 12 is fitted with an escape or pressurised gas discharge valve 28.
Similarly, intermediate storage tank 13 is also fitted with a valve 29 having the same functions.
The operating principle of the device according to the invention is as follows: the two intermediate storage tanks 12 and 13 are alternately filled and emptied.
While one of the tanks is emptied via the discharge line, by the corresponding relief valve, the other intermediate storage tank is filled. The emptying of the first tank is controlled as a function of the w6ight loss measured by means of the weighing machine corr esponding to the respective tank. The regulation of the discharge of the liquid or thick substances con tained in the tank is effected by controlling the pressure of the gas injected into said tank. This gas may be a neutral gas, a mixture of gas, air, steam or any other gas not reacting with the substances contained in the tank. The regulation may also be effected by controlling the relief valve which is advantageously formed by a pneumatic 0-ring.
When the substances to be metered are formed by easily flowing liquids, the supply vat is connected to the intermediate storage tank and the liquid flows by grav ity into said tank, the section of the supply line being chosen so that the tank is filled over a period of time substantially equal to 80 % of the minimum time required to ensure the other tank is emptied. On the other hand, if the substance contained in the supply vat is viscous or thick, this vat is pressurised to ensure the forced filling of the intermediate storage tanks. The filling of these intermediate storage tanks 12 and 13 is facil itated by two escape valves 28 and 29 ensuring the re moval of the air initially contained in the tank, at the moment of this filling. The tank containing a pre determined volume of substance to be metered is w6ighed; when the upper level is reached, the supply valve is closed.
At the same time the other intermediate storage tank was emptied as a preliminary, this emptying being con trolled as a function of the weight loss of the tank, which is measured by the corresponding weighing machine.
6 This regulation is carried out by controlling the pressure of the gas injected into the intermediate storage tank during the emptying operation, and the said pressure is intended more or less to force sub s stance towards the relief valve. Bearing in mind the elasticity of the gases, this method may have a tendency to vary with respect to the flow if the variations are rapid. However it has the advantage of not having any moving part in contact with the liquid, and this removes any risk of pollution.
Furthermore relief and/or control valves 22 and 23 preferably comprise a circular aperture closed by a holl ow 0-ring made of elastic material and supplied with a liquid which can be injected under pressure. The opening of the relief valve is directly associated with the pressure of the liquid injected into said ring.
It is clearly understood that these relief valves having a pneumatic ring could be replaced by a needlp valve or any other equivalent device. It is also possible to place a single control valve 19 on outlet line 18, in this case the only function of valves 22 and 23 being to shut. As above, no moving part dis turbs the liquid as it is drained from the tank be ing emptied.
It is as well to note that the pressurising of the intermediate storage tank being emptied does not sig nificantly influence the weight of said tank. In fact, the weight of the volureof pressurised air or gas injected into the tank is practically negligible.
with respect to the weight of the liquid or thick substance contained in said tank. For this reason it is possible to regulate the weight loss of the tank during emptying.
7 When the tank being emptied reaches the lower level, an automatic control and operating device 30 ensures the switching of supply and relief valves so that a new filling and emptying cycle can be started.
To carry out metering, the following procedure is used:
- the supply valve of the previously filled inter- mediate tank is closed, - the escape valve of this tank is opened, - the tank is pressurised, - a chain for measuring the weight of the two tanks is activated, - the relief valve of the filled tank is progress- ively opened and the relief valve of the emptied tank is progressively closed, - the chain for measuring the weight of the filled tank is activated, - the inlet of the pressurised gas into the empty tank is closed, - the supply valve of the empty tank is opened, - the weight of this tank is regulated as it is filled so as to ascertain the moment when it is regarded as being full.
- and the corresponding supply valve is closed.
It is obvious that if the installation only has a single intermediate storage tank, it is hardly possible to ensure the continuous metering of substances in- itially contained in supply vat 10. The preferred refinement comprises two intermdiate storage tanks.
one of which is being filled while the other is being emptied and enables continuous metering of substances 11 to be ensured.
8 As mentioned above, this installation and the pro- cess which it ensures enables liquid or thick sub- stances to be metered without the use of a pump.
This invention is not limited to the embodiments described above but may undergo various modifications and may be presented in various ways obvious for a person skilled in the art. Inter alia, the weighing machine may be replaced by measuring the flow in line by -the control valve, by an ultrasonic or Corriolis ef f ect flowmeter or by any other appliance. Furthermore, it will be noted that if the substances treated so require, it is also possible to provide the install ation with a thermostat. This is particularly ad vantageous if viscous substances have to be treated at ambient temperature. This installation enables liquids to be "pumped" upwards. It also enables dangerous liquids and explosive substances-to be treated by appropriately dimensioning the vat and the intermediate tanks.
9

Claims (12)

Claims
1. Process for metering liquid or thick substances, characterised in that predetermined masses or volumes of these substances are sequentially tapped, in that these predetermined masses or volumes are temporarily stored in at least one intermediate storage tank of known weight and /or volume, in that these predeterm ined masses or volumes are.subjected to the pressure of a gas and in that the opening of a relief valve and/or the pressure of said gas in said tank is reg ulated so that the flow of said predetermined masses or volumes occurs within a given time.
2. Process according to Claim 1, characterised in that two intermediate storage tanks arranged in parallel are used and in that one of these intermediate storage tanks is filled during At most a part of the time required to empty the other tank.
3. Process according to Claim 2, characterised in that means for filling and emptying these intermediate storage tanks are designed so that one of these tanks can be filled within a period of time less thc,n the minimum time required to empty the other tank.
4. Process according to Claim 1, characterised in that the weight of said predetermined masses of sub stances is determined by weighing the tank.
5. Process according to any one of the above claims, characterised in that, while the tank is being emptied, the variation in weight of the tank containingsubstances to be metered is regulated continuously and in that the discharge flow of these substances is regulated by adjusting the pressure of the gas injected into the tank and/or the opening of the relief valve.
- lO -
6. Process according to Claim 1, characterised in that metering is carried out as follows:
- the supply valve of the previously filled inter- mediate tank is closed, - the escape valve for this tank is opened, - the tank is pressurised, - a chain for measuring the weight of the two tanks is activated, - the relief valve of the filled tank is progressively opened and the relief valve of the emptied tank is progressively closed, - the chain for measuring the weight of the filled -- tank is activated, - the inlet of the pressurised gas into the empty tank is closed, - the supply valve of the empty tank is opened, - the weight of this tank is regulated as it is filled so as to ascertain the moment when it is regarded as being full, - and the corresponding supply valve is closed.
7. Installation for metering liquid or thick substances, enabling the process according to any one of the above claims to be carried out, comprising a supply vat (10) containing the substances (11) to be metered, means for tapping predetermined masses or volumes of these sub stances, and means for the controlled discharge of said predetermined masses or volumes, characterised in that the means for tapping said predetermined masses or volumes and the means for discharging them comprise at least one intermediate storage tank (12 or 13), a pressurised gas generating device (24)-for putting the substances contained in this tank under the pressure of this gas, at least one relief and/or control valve (22 or 23) mounted on a discharge line (16 or 17) of this tank and control and operating elements (30) for the pressurised gas generator and of the relief and/or control valve (22 or 23).
8. Installation according to Claim 7, character ised in that it comprises two intermediate storage tanks (12 and 13) connected in parallel to the supply vat (10) and a discharge circuit comprising two relief and control valves (22, 23) respectively conn ected to each 'of the two tanks.
9. Installation according to Claim 7, character ised in that it comprises two intermediate storage tanks (12 and 13) connected in parallel to the supply vat (10) and a discharge circuit comprising two relief valves (22, 23) respectively connected to each of the two tanks and a single control valve (19).
10. Installation according to Claim 7, character ised in that each intermediate storage tank is connected to a weighing machine (26, 27) for measuring the weight of this tank containing a predetermined mass of the substance to be metered.
11. Installation according to any one of the above claims, characterised in that the control valves (22, 23, 19) are of the type having a pneumatic 0-ring.
12. A process for metering liquid or thick substances, or an installation enabling the process to be carried out, substances hereinbefore described with reference to the accompanying drawing.
Published 1988 at The Patent Office, State House, 66/71 High Holborn, London WClR 4TP. Purther copies may be obtained from The Patent Office, Sales Branch, St Mary Cray, Orpington, Kent BR5 3RD. Printed b.v Multiplex tecbniaues ltd. St Marv Crav. Kent. Con. 1/87.
GB08809110A 1987-05-05 1988-04-18 Metering liquid or thick substances Withdrawn GB2204363A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8706441A FR2614983A1 (en) 1987-05-05 1987-05-05 METHOD FOR DETERMINING LIQUID OR PASSIZED SUBSTANCES AND INSTALLATION FOR CARRYING OUT SAID METHOD

Publications (2)

Publication Number Publication Date
GB8809110D0 GB8809110D0 (en) 1988-05-18
GB2204363A true GB2204363A (en) 1988-11-09

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ID=9350868

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08809110A Withdrawn GB2204363A (en) 1987-05-05 1988-04-18 Metering liquid or thick substances

Country Status (4)

Country Link
DE (1) DE3815034A1 (en)
FR (1) FR2614983A1 (en)
GB (1) GB2204363A (en)
IT (1) IT1217413B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5242272A (en) * 1989-08-10 1993-09-07 Kari Ven Method and device for pumping a liquid at high temperature through a pipe
GB2350434A (en) * 1999-03-23 2000-11-29 Admix Water Serv Ltd Metering liquid additives by weight
WO2012075354A1 (en) * 2010-12-02 2012-06-07 The Coca-Cola Company Gravity fed beverage dispenser

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3841785A1 (en) * 1988-12-12 1990-06-13 Vinko Hartli Apparatus for metering liquids
DE102009016963B4 (en) * 2009-04-14 2014-10-02 Porep Gmbh Device for flow measurement of lubricants
CN113588048B (en) * 2021-08-16 2023-10-31 中国空气动力研究与发展中心设备设计与测试技术研究所 Method for calibrating mass flow in site by using volumetric flowmeter

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB734068A (en) * 1952-09-05 1955-07-20 Aer Rianta Teoranta Apparatus for converting a low pressure supply of liquid into a conti high pressure supply of liquid by the use of compressed air
GB1020019A (en) * 1963-08-21 1966-02-16 Plenty & Son Ltd Improvements in or relating to apparatus for continuously supplying a mixture of liquid and solid materials at a constant rate
GB1390982A (en) * 1972-03-20 1975-04-16 Faldi G Pump used in dredging systems operating with compressed air
GB1421434A (en) * 1972-03-20 1976-01-21 Faldi G Apparatus for conveying materials comprising liquids containing solid material
GB1491717A (en) * 1973-11-01 1977-11-16 Wolff R Liquid transfer system
GB1603764A (en) * 1978-05-23 1981-11-25 Gillilan J Power generating system

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR947663A (en) * 1947-05-21 1949-07-08 Method and apparatus for rapid gauging of liquids
DE2821372C2 (en) * 1978-05-16 1986-02-27 Andreas Von Dipl.-Rer.Pol. Bennigsen-Mackiewicz Device for dispensing measured amounts of fine-grained bulk material
FR2470368A1 (en) * 1979-11-22 1981-05-29 Sp K Bjuro Quantitative fluid measurement - involves synchronised filling and weighing, and emptying of containers without interrupting flow
FI66202C (en) * 1981-11-17 1984-09-10 Outokumpu Oy FOER FARERE OCH ANORDNING FOER ATT PNEUMATISKT MATA TILLSATSMATERIALIER TILL KONVERTRAR

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB734068A (en) * 1952-09-05 1955-07-20 Aer Rianta Teoranta Apparatus for converting a low pressure supply of liquid into a conti high pressure supply of liquid by the use of compressed air
GB1020019A (en) * 1963-08-21 1966-02-16 Plenty & Son Ltd Improvements in or relating to apparatus for continuously supplying a mixture of liquid and solid materials at a constant rate
GB1390982A (en) * 1972-03-20 1975-04-16 Faldi G Pump used in dredging systems operating with compressed air
GB1421434A (en) * 1972-03-20 1976-01-21 Faldi G Apparatus for conveying materials comprising liquids containing solid material
GB1491717A (en) * 1973-11-01 1977-11-16 Wolff R Liquid transfer system
GB1603764A (en) * 1978-05-23 1981-11-25 Gillilan J Power generating system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5242272A (en) * 1989-08-10 1993-09-07 Kari Ven Method and device for pumping a liquid at high temperature through a pipe
GB2350434A (en) * 1999-03-23 2000-11-29 Admix Water Serv Ltd Metering liquid additives by weight
WO2012075354A1 (en) * 2010-12-02 2012-06-07 The Coca-Cola Company Gravity fed beverage dispenser

Also Published As

Publication number Publication date
IT1217413B (en) 1990-03-22
DE3815034A1 (en) 1988-11-17
FR2614983A1 (en) 1988-11-10
IT8820194A0 (en) 1988-04-13
GB8809110D0 (en) 1988-05-18

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WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)