DE29622800U1 - Device for recording the liquid gas transfer - Google Patents
Device for recording the liquid gas transferInfo
- Publication number
- DE29622800U1 DE29622800U1 DE29622800U DE29622800U DE29622800U1 DE 29622800 U1 DE29622800 U1 DE 29622800U1 DE 29622800 U DE29622800 U DE 29622800U DE 29622800 U DE29622800 U DE 29622800U DE 29622800 U1 DE29622800 U1 DE 29622800U1
- Authority
- DE
- Germany
- Prior art keywords
- tank
- gas
- recording
- per unit
- time
- 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.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims description 9
- 230000010354 integration Effects 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 238000005259 measurement Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000009529 body temperature measurement Methods 0.000 description 1
- 244000309464 bull Species 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
- F17C13/028—Special adaptations of indicating, measuring, or monitoring equipment having the volume as the parameter
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
- G01F1/76—Devices for measuring mass flow of a fluid or a fluent solid material
- G01F1/86—Indirect mass flowmeters, e.g. measuring volume flow and density, temperature or pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0439—Temperature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0443—Flow or movement of content
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0486—Indicating or measuring characterised by the location
- F17C2250/0495—Indicating or measuring characterised by the location the indicated parameter is a converted measured parameter
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0621—Volume
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- General Physics & Mathematics (AREA)
- Gas Separation By Absorption (AREA)
Description
Gerät zur Erfassung der FlüssiggasübergabeDevice for recording the liquid gas transfer
Die Erfindung bezieht sich auf ein Gerät zur Erfassung einer Flüssiggas-Übergabemenge von einem ersten Tank zu einem zweiten Tank unter Rückführung von Gas aus dem zweiten Tank in den ersten Tank als Polstergas.The invention relates to a device for detecting a liquid gas transfer quantity from a first tank to a second tank while returning gas from the second tank to the first tank as cushion gas.
Die Übergabe von Flüssiggas ist z.B. bei der Umfüllung aus Eisenbahntankwagen in stationäre Behälter, bei der Be- und Entladung von Gastankern und ähnlichen Anlagen erforderlich. In Zukunft kann evtl. auch eine Flugzeugbetankung infrage kommen.The transfer of liquefied gas is necessary, for example, when transferring from rail tankers to stationary containers, when loading and unloading gas tankers and similar facilities. In the future, aircraft refueling may also be an option.
In vielen Fällen kann aus den unterschiedlichsten Gründen nicht gewogen werden, aber es sollte trotzdem eine eindeutige Aussage über die Menge des übergebenen Gases gemacht werden können.In many cases, weighing is not possible for a variety of reasons, but it should still be possible to make a clear statement about the amount of gas transferred.
. Die Aufgabe der vorliegenden Erfindung besteht demnach darin, ein Gerät zu schaffen, mit dem ohne direkte Gewichtsmessung die effektive Flüssiggas-Übergabemenge erfaßt werden kann.. The object of the present invention is therefore to create a device with which the effective liquid gas delivery quantity can be recorded without direct weight measurement.
Die Lösung der Aufgabe geschieht bei einem eingangs genannten
Gerät in der Weise, daß
a) eine Erfassung des Durchflußvolumens je Zeiteinheit vom ersten zum zweiten Tank und vom zweiten zum ersten TankThe solution to the problem is achieved with the device mentioned above in such a way that
a) a recording of the flow volume per unit of time from the first to the second tank and from the second to the first tank
vorgesehen ist,is provided,
9€ G 3599 DE9€ G 3599 DE
b) eine Erfassung der Temperatur des vom ersten zum zweiten und vom zweiten zum ersten Tank strömenden Gases vorgesehen ist,b) the temperature of the gas flowing from the first to the second and from the second to the first tank is measured ,
c) ferner eine Berechnung der damit verknüpften Gasmengen je Zeiteinheit vorgesehen ist und(c) furthermore, a calculation of the associated gas quantities per unit of time is provided for and
d) eine Bildung der Differenz der Gasmenge und der Integration der Differenz über die Übergabedauer vorgesehen ist.d) the calculation of the difference in the gas quantity and the integration of the difference over the transfer period is provided for.
Auf diese Weise erhält man z.B. die gelieferte Gasmenge in Tonnen. Je nach Gasart und Genauigkeitsannahmen kann man dabei das Gas als ideales Gas oder als reales Gas betrachten und dabei Grenzwerte berücksichtigen. Der ganze Rechenvorgang ist zweckmäßigerweise in einem frei programmierbaren Steuergerät vornehmbar, dem die entsprechenden Werte von Druck, Temperatur usw. zugeführt werden. Kostenmäßig ist dabei die Verwendung eines einfachen Standard-Automatisierungsgerätes, z.B. des Gerätes SIPART DR 24 der Firma Siemens AG, am günstigsten. Dieses Gerät wurde für einfache Steuerungen und Re-0 gelaufgaben konzipiert, überraschenderweise ist es jedoch bei entsprechender Programmierung auch für die Lösung der erfindungsgemäßen Aufgabe verwendbar.In this way, for example, the amount of gas delivered can be obtained in tons. Depending on the type of gas and the assumptions about accuracy, the gas can be considered as an ideal gas or as a real gas and limit values can be taken into account. The entire calculation process can be carried out in a freely programmable control device to which the corresponding values of pressure, temperature, etc. are fed. In terms of cost, the use of a simple standard automation device, e.g. the SIPART DR 24 device from Siemens AG, is the cheapest. This device was designed for simple control and regulation tasks, but surprisingly, with appropriate programming, it can also be used to solve the task according to the invention.
Anhand eines in der Zeichnung dargestellten Ausführungsbeispiels sei die Erfindung näher erläutert:The invention is explained in more detail using an embodiment shown in the drawing:
Wie aus der Zeichnung ersichtlich, wird aus einem Kesselwagen 1 über eine Kesselwagenentladepumpe 2 Flüssiggas entnommen und einem Tank 3 zugeführt. Aus diesem Tank 3 wird über einenAs can be seen from the drawing, liquid gas is taken from a tank wagon 1 via a tank wagon unloading pump 2 and fed to a tank 3. From this tank 3, liquid gas is
GR 96 G 3599 DEGR 96 G 3599 EN
• · ♦··· ♦·• · ♦··· ♦·
Kompressor 4 Polstergas 5 in den Kesselwagen 1 zurückgeführt, um hier Explosionszustände zu vermeiden.Compressor 4 cushion gas 5 is returned to the tank car 1 in order to avoid explosion conditions.
Für das vom Kesselwagen 1 zum Tank 3 strömende Gas sind Geräte 6 zur Volumenmessung und 7 zur Temperaturmessung vorgesehen. Ferner sind für das Polstergas Erfassungseinrichtungen 8 für Druck, 9 für Volumen und 10 für Temperatur vorhanden. Die entsprechenden Werte für Temperatur Tl und Volumen Vl des vom Kesselwagen 1 zum Tank 3 strömenden Flüssiggases 1 werden einem Grenzkurvenrechner 12, z.B. dem erwähnten Gerät SIPART DR 24, zugeführt, der die je Zeiteinheit strömende Gasmenge in Normkubikmetern pro Stunde bestimmt. Die Ausgangskurve dieses Rechners kann vorteilhaft dabei nichtlinear sein.For the gas flowing from the tank wagon 1 to the tank 3, devices 6 for volume measurement and 7 for temperature measurement are provided. In addition, recording devices 8 for pressure, 9 for volume and 10 for temperature are available for the cushioning gas. The corresponding values for temperature Tl and volume Vl of the liquid gas 1 flowing from the tank wagon 1 to the tank 3 are supplied to a limit curve calculator 12, e.g. the SIPART DR 24 device mentioned above, which determines the amount of gas flowing per unit of time in standard cubic meters per hour. The output curve of this calculator can advantageously be non-linear.
Die entsprechenden Werte des zurückströmenden Polstergases 5, d.h. Druck P2 Volumen V2 und Temperatur T2 werden einem einfachen Rechner 11 für ideales Gas zugeführt, und hieraus die gelieferte Gasmenge pro Zeiteinheit berechnet. Gleichzeitig werden diese Daten auch einem Grenzkurvenrechner 13, z.B. dem 0 erwähnten SIPART DR 24, zugeführt, der unter bestimmten Voraussetzungen an Stelle des einfachen Rechners 11 oder Rechnerteils benutzt werden kann. Die Auswahl zwischen den beiden Rechnern oder Rechnerteilen geschieht durch einen Umschalter 14. Die gewonnenen Werte werden in einem Baustein 15 auf Flüssiggas umgerechnet. Anschließend wird in einem Differenzbildner 16 die je Zeiteinheit strömende Differenz der hin- und herströmenden Gasmengen berechnet, und zwar in Normkubikmetern pro Stunde, d.h., in Gasmengen je Zeiteinheit. Diese Gasmengen werden in einen Integrator 17 integriert, d.h., 0 hier ergeben sich die gelieferten Gasmengen-Normkubikmeter.The corresponding values of the backflowing cushion gas 5, i.e. pressure P2, volume V2 and temperature T2 are fed to a simple computer 11 for ideal gas, and from this the amount of gas delivered per unit of time is calculated. At the same time, these data are also fed to a limit curve calculator 13, e.g. the SIPART DR 24 mentioned above, which can be used under certain conditions instead of the simple calculator 11 or calculator part. The selection between the two computers or calculator parts is made by a switch 14. The values obtained are converted to liquid gas in a module 15. The difference between the gas quantities flowing back and forth per unit of time is then calculated in a difference generator 16, namely in standard cubic meters per hour, i.e. in gas quantities per unit of time. These gas quantities are integrated in an integrator 17, i.e., 0 this results in the standard cubic meters of gas quantities delivered.
GR 96 G 3599 DEGR 96 G 3599 EN
Die Steuerung dieses Vorganges kann durch Zähler 18 und vorgenommen werden. Die gelieferte Gasmenge in Normkubikmetern wird dann vorteilhafterweise noch in einer Einrichtung 20 in Tonnen umgerechnet und dann in einer Anzeige 21 mit entsprechendem Kontrollausdruck angezeigt.This process can be controlled by counters 18 and . The gas quantity delivered in standard cubic meters is then advantageously converted into tons in a device 20 and then shown in a display 21 with a corresponding control printout.
Die vorstehend erwähnten einzelnen Bausteine sind in der realen Ausführung normalerweise in einem Rechner oder in einem freiprogrammierbaren Steuergerät realisiert. Nur der Verständlichkeit halber werden sie in Einzelbausteine auseinandergezogen .In their actual form, the individual modules mentioned above are normally implemented in a computer or in a freely programmable control unit. They are broken down into individual modules for the sake of clarity.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29622800U DE29622800U1 (en) | 1996-08-07 | 1996-08-07 | Device for recording the liquid gas transfer |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29622800U DE29622800U1 (en) | 1996-08-07 | 1996-08-07 | Device for recording the liquid gas transfer |
DE19631927 | 1996-08-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
DE29622800U1 true DE29622800U1 (en) | 1997-07-10 |
Family
ID=26028211
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE29622800U Expired - Lifetime DE29622800U1 (en) | 1996-08-07 | 1996-08-07 | Device for recording the liquid gas transfer |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE29622800U1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000057325A2 (en) * | 1999-03-19 | 2000-09-28 | Micro Motion, Inc. | Batch maximization for a batch delivery system |
DE10010193A1 (en) * | 2000-03-02 | 2001-09-20 | Messer Italia S P A | Filler of liquid gas into container, has conveyor, storage tank, gas discharge pipe, pump stages, and flow connection |
WO2006015927A1 (en) * | 2004-08-07 | 2006-02-16 | Messer France S.A. | Method and device for filling a container with liquid gas from a storage tank |
WO2017134407A1 (en) * | 2016-02-04 | 2017-08-10 | Cryostar Sas | Cryogenic liquid delivery system |
CN108431487A (en) * | 2015-10-05 | 2018-08-21 | 克里奥斯塔股份有限公司 | Method for transferring a cryogenic liquid and device for carrying out said method |
-
1996
- 1996-08-07 DE DE29622800U patent/DE29622800U1/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000057325A2 (en) * | 1999-03-19 | 2000-09-28 | Micro Motion, Inc. | Batch maximization for a batch delivery system |
WO2000057325A3 (en) * | 1999-03-19 | 2002-01-10 | Micro Motion Inc | Batch maximization for a batch delivery system |
DE10010193A1 (en) * | 2000-03-02 | 2001-09-20 | Messer Italia S P A | Filler of liquid gas into container, has conveyor, storage tank, gas discharge pipe, pump stages, and flow connection |
WO2006015927A1 (en) * | 2004-08-07 | 2006-02-16 | Messer France S.A. | Method and device for filling a container with liquid gas from a storage tank |
CN108431487A (en) * | 2015-10-05 | 2018-08-21 | 克里奥斯塔股份有限公司 | Method for transferring a cryogenic liquid and device for carrying out said method |
CN108431487B (en) * | 2015-10-05 | 2020-08-11 | 克里奥斯塔股份有限公司 | Method for transferring a cryogenic liquid and device for carrying out said method |
WO2017134407A1 (en) * | 2016-02-04 | 2017-08-10 | Cryostar Sas | Cryogenic liquid delivery system |
CN109073152A (en) * | 2016-02-04 | 2018-12-21 | 克里奥斯塔股份有限公司 | Cryogenic liquid delivery system |
RU2730213C2 (en) * | 2016-02-04 | 2020-08-19 | Криостар Сас | Cryogenic liquid supply device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
R207 | Utility model specification |
Effective date: 19970821 |
|
R150 | Utility model maintained after payment of first maintenance fee after three years |
Effective date: 20000128 |
|
R151 | Utility model maintained after payment of second maintenance fee after six years |
Effective date: 20021204 |
|
R158 | Lapse of ip right after 8 years |
Effective date: 20050301 |