The present disclosure relates in general to the distribution of liquids, and specifically to measurement of liquid dispensed from a container.
In the oilfield industry, a variety of liquids may be utilized during many operations used in drilling, completing, and producing a well. For example, liquid used during hydraulic fracturing operations may include a variety of chemicals used to, for example, reduce friction, reduce surface effects, or otherwise affect the downhole formation during a fracturing process. Suppliers of these liquids may utilize Intermediate Bulk Containers to transport liquids to and between wellsites. Liquids are generally sold by volume used, and a given wellsite may only use a portion of the liquid supplied. Typically, volume used must be determined on site by direct measurement of fluid levels in the containers.
The present disclosure provides for a system for determining the amount of liquid dispensed from a fluid container. The system may include a fluid container, the fluid container at least partially filled with a liquid, the remainder of the interior of the fluid container filled with a gas. The fluid container may include at least one drain outlet positioned to allow the liquid to be dispensed from the fluid container. The fluid container may include a pressure transducer positioned to measure the differential pressure between the gas or the liquid and the surrounding environment. The system may include a control unit positioned to receive a differential pressure signal from the pressure transducer and positioned to calculate the volume of liquid dispensed.
The present disclosure also provides for a method of measuring a volume of a liquid dispensed. The method may include filling, at least partially, a fluid container with a liquid, the remainder of the interior of the fluid container filled with a gas, the fluid container including at least one drain outlet positioned to allow the liquid to be dispensed from the fluid container, the fluid container including a pressure transducer positioned to measure the differential pressure between the gas or the liquid and the surrounding environment; reading the differential pressure from the pressure transducer to determine an initial pressure; dispensing at least a portion of the liquid from the fluid container; reading the differential pressure from the pressure transducer to determine a second pressure; calculating the volume of liquid dispensed.
The present disclosure is best understood from the following detailed description when read with the accompanying figures. It is emphasized that, in accordance with the standard practice in the industry, various features are not drawn to scale. In fact, the dimensions of the various features may be arbitrarily increased or reduced for clarity of discussion.
It is to be understood that the following disclosure provides many different embodiments, or examples, for implementing different features of various embodiments. Specific examples of components and arrangements are described below to simplify the present disclosure. These are, of course, merely examples and are not intended to be limiting. In addition, the present disclosure may repeat reference numerals and/or letters in the various examples. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various embodiments and/or configurations discussed.
As depicted in
Control unit 111 may be positioned to measure the differential pressure as output by each fluid container 101, allowing control unit 111 to calculate the volume of liquid remaining in each fluid container 101. In some embodiments, flatbed 10 may include a suspension system positioned to ensure any fluid containers 101 are level at the time of reading. In some embodiments, the suspension system may be an active suspension including, for example and without limitation, an air suspension system.
In some embodiments, control unit 111 may include a display to display relevant data to a user including, for example and without limitation, starting liquid volume, current liquid volume, change in liquid volume, time of delivery, time of current and previous measurement, etc. In some embodiments, control unit 111 may include a printer to print, for example, a ticket, invoice, or receipt for the liquid used. In some embodiments, control unit 111 may output or print readings or measurements on demand and/or according to a schedule. In some embodiments, control unit 111 may include a data port capable of being connected to a wellsite network. In some embodiments, the data port may be, as understood in the art, an RS 232 compatible connection.
In some embodiments, control unit 111 may be powered by a battery. In some embodiments, the battery may be recharged by a solar array. In some embodiments, the battery may be recharged by a wind turbine. In some embodiments, control unit 111 may also be capable of providing a closed pressure system. In some such embodiments, control unit 111 may be positioned to control a pump or to control a valve on a compressed gas container each positioned to provide pressurized gas to fluid container 101 to, for example, fill space in fluid container 101 left by dispensed fluid or to force fluid from fluid container 101.
In some embodiments, the combined gas law may be utilized to determine the amount of liquid that has been dispensed since the last time fluid container 101 was connected to control unit 111 by measuring, as depicted in
where P1 is the pressure of gas 113, V1 is the volume of the gas, T1 is the temperature of the gas, and k is a constant. The constant k remains the same value while conditions, such as pressure, volume, and temperature vary. Thus, extending the combined gas law to apply to a second set of parameters, the following equations may be derived:
where P2, V2, and T2 are the pressure, volume, and temperature of gas 113 at the second point in time.
Assuming that fluid container 101 is sealed at the time it is filled by the supply depot and no additional gas may enter thereinto, by measuring the change in pressure of gas 113 between the filled state and the at least partially emptied state (as well as the temperature change), the corresponding volume of liquid 115 dispensed may be calculated. The equation to do so may be derived as follows:
where Vcontainer is the volume of the container, ΔVgas and ΔVfluid are the change in volume of the gas and liquid respectively, Vliquid,filled is the volume of liquid in fluid container 101 when fluid container 101 is delivered to the wellsite, and Pfilled, Tfilled, Pemptied, and Vemptied are the pressures and volumes of the gas when fluid container 101 is delivered (filled) and picked up (emptied). Thus, by measuring the change in pressure of gas 113 with a known volume of liquid 115 in a fluid container 101 of known volume, the amount of liquid 115 dispensed may be calculated. In some embodiments, the temperature term may be ignored, assuming that gas 113 is air, and the temperature of the gas is the same as the temperature of the surrounding environment both when fluid container 101 is filled and when the measurement is taken.
In some embodiments, the hydrostatic pressure of liquid within the container may instead be utilized. As depicted in
In embodiments measuring the hydrostatic pressure of liquid 215, the height of the column of liquid 215 may be calculated from the differential pressure measured by hydrostatic pressure sensor 205. Assuming that liquid 215 is incompressible, and thus the density of liquid 215 is constant, the height of liquid 215 above hydrostatic pressure sensor 205 may be calculated according to:
where h is the height of liquid 215 above hydrostatic pressure sensor 205, p is the differential pressure measured by hydrostatic pressure sensor 205, g is the gravitational acceleration, and ρ is the density of the fluid. One having ordinary skill in the art with the benefit of this disclosure will understand that the density of liquid 215 may be calculated from its specific gravity, and that the density of liquid 215 may vary based on, for example, the temperature of liquid 215. By knowing the height of liquid 215 and the geometry of fluid container 201, the volume of liquid 215 in fluid container 201 may be calculated according to:
V=∫
0
h
A(z)dz,
where V is the volume of liquid 215 above hydrostatic pressure sensor 205, z is a distance in the direction of h (up) from hydrostatic pressure sensor 205, and A(z) is the cross-sectional area of fluid container 201 at a distance z. By comparing the volume of liquid 215 measured at drop off and the volume of liquid 215 measured at pick-up, the volume of liquid 215 dispensed can be readily calculated.
With regards to
Once measurements are received at portal 117, portal 117 may initiate a billing request from the client. In some embodiments, each fluid container 101 may be assigned a unique identifier such as a serial number to allow portal 117 to associate the fluid container 101 with a specific client, worksite, liquid type, distributor, etc. Portal 117 may, in some embodiments, aggregate this data to identify the client, worksite, container, liquid type, distributor, and automatically generate a bill for the client based on the amount of liquid dispensed as calculated by control unit 111. In some embodiments, a user input on control unit 111 may cause control unit 111 to measure pressure differential and transmit the information to portal 117.
In other embodiments, rather than utilizing pressure sensor 105 to determine the amount of liquid dispensed from fluid container 101, a load cell may be used to determine the weight of fluid container 101, and thus derive the amount of liquid dispensed by comparing the weight of fluid container 101 at delivery and when picked up. Knowing the density or specific gravity of the liquid, the volume dispensed may be calculated. Such a load cell may be positioned on flatbed 10 or as a part of fluid container 101.
The foregoing outlines features of several embodiments so that a person of ordinary skill in the art may better understand the aspects of the present disclosure. Such features may be replaced by any one of numerous equivalent alternatives, only some of which are disclosed herein. One of ordinary skill in the art should appreciate that they may readily use the present disclosure as a basis for designing or modifying other processes and structures for carrying out the same purposes and/or achieving the same advantages of the embodiments introduced herein. One of ordinary skill in the art should also realize that such equivalent constructions do not depart from the spirit and scope of the present disclosure and that they may make various changes, substitutions, and alterations herein without departing from the spirit and scope of the present disclosure.
This application is a non-provisional application which claims priority from U.S. provisional application No. 61/940,080, filed Feb. 14, 2014, which is incorporated by reference herein in its entirety.
Number | Date | Country | |
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61940080 | Feb 2014 | US |