The field of the disclosure relates generally to systems of a multiple pump manifold with to provide redundancy in gas extraction systems, and more particularly, to systems and methods that include a multiple pump manifold to provide redundancy for use with high availability gas extraction system in industrial instrumentation.
Whenever fuel gas such as natural gas, coal syngas, or biogas, is generated, transferred, or used, an assessment and understanding of the levels of contaminants is typically required in order to effectively transfer or use the desired fuel gas in an associated process. The measurement of various contaminants, e.g., H2S, H2O, O2, and CO2, is an important process step that aids in the prevention of infrastructure damage due to corrosion or chemical reactivity that in-part is a product of fuel gas contaminants. Natural gas producers must clean extracted gas to remove contaminants and then verify residual contaminant levels before introducing natural gas into a pipeline. Desulfurizer bed, used as fuel reformers to remove a variety of fuel gas contaminants must be periodically replaced or regenerated to prevent H2S breakthrough into the reformed fuel product, reinforcing the need for frequent contaminant level monitoring in fuel gas.
The systems and instruments for measurement of contaminants are often stored in inaccessible and harsh environments. Such systems require continuous control of the flow and pressure of the component that is to be measured. Pumps are used to deliver the controlled flow at a stable under-pressure. However, pumps and pumping systems have a limited lifetime, limiting the reliability of the measurement system. Because the volume of gas in the extraction system can be significant, when a pump fails, the measurement response times, and accuracy will be negatively impacted which will yield the consumption (and exhaust to atmosphere) of relatively large volumes of fuel gas. Continuous operation of the system is essential in preventing catastrophic failure of the instrumentation and of the pipeline.
Therefore, there exists a need in the art to provide for a pump manifold with redundancies for gas extraction systems and instrumentation.
In one aspect, a method of operating a redundant pump assembly is disclosed. The method includes operating a first pump of a plurality of pumps for an operation period; validating a second pump of the plurality of pumps at the end of the operation period of the first pump; validating a third pump of the plurality of pumps at the end of the operation period of the first pump; and, operating the third pump for the operation period, where the second pump and third pump are validated as operational.
In another aspect, redundant pump manifold assembly for use with a measurement instrument is disclosed. The assembly includes a first plate having a first surface and a second surface defining a thickness of the first plate, the second surface including a plurality of channels extending into the second surface, and a first aperture and second aperture extending from the plurality of channels to the first surface; and, a second plate having a first surface and a second surface defining a thickness of the first plate, the first surface of the second plate abutting the second surface of the first plate, wherein the first surface of the second plate includes a recessed surface for receiving a gasket positioned between the first plate and second plate creating a fluid seal between the first plate and second plate. The corresponding protrusions extend from the recessed surface of the second plate, the corresponding protrusions configured to align with the plurality of channels.
These and other features, aspects, and advantages of the present disclosure will become better understood when the following detailed description is read with reference to the accompanying drawings in which like characters represent like parts throughout the drawings.
In the following specification and the claims, reference will be made to a number of terms, which shall be defined to have the following meanings.
As used herein, the singular forms “a,” “an,” and “the” include plural references unless the context clearly dictates otherwise. The terms “comprising,” “including,” and “having” are intended to be inclusive and mean that there may be additional elements other than the listed elements. The terms “optional” or “optionally” means that the subsequently described event or circumstance may or may not occur, and that the description includes instances where the event occurs and instances where it does not.
Measurement of various contaminants, e.g. Hydrogen Sulfide (H2S), Water (H2O), Oxygen (O2), and Carbon Dioxide (CO2), in fuel gas is needed for preventing infrastructure damage and for compliance with operation requirements. Corrosion from H2S, CO2, H2O and O2 negatively impacts the integrity of associated delivery infrastructure and the degradation of the infrastructure may result in cracks or other openings that enable the fuel gas to leak undesirably to downstream assets. H2S is deadly even at low parts per million (ppm) values. Excess H2O leads to hydrates that decrease flow capacity and potential blockage. Excess O2 degrades gas processing chemicals such as amines. In addition, H2S, CO2, H2O and O2 do not comprise fuel gas components that enhance the inherent combustibility of the fuel gas, and therefore may be removed from fuel gases.
Gas extraction systems are configured to control pressure and flow to a fuel gas analysis cell. The analysis cells are designed to operate with a high degree of availability and uninterrupted measurement performance. Interruptions in analysis cell performance/analysis cell down time can occur for example due to pump failure, leakage of the measurement assembly or pump assembly and leakage between tubing, fittings, and components of the measurement system generally. Embodiments of the present disclosure are directed to a pump manifold having built in redundancy and periodic validation of pump health and performance incorporated into a modular primary manifold which minimizes tubing and tube fittings to minimize leaks, minimizes the envelope of the system and has fast response time and for easy replacement. The embodiments of the present disclosure will maximize operation of the analysis cells by minimizing analysis cell down time due to pump failure.
The flame arrester module 110, pinole holder module 150, measurement instrument module 160, and redundant pump manifold assembly 300 are modularly connected to the main manifold 200 (and are hereinafter referred to as “modular components”). A surface of each of the modular components directly contacts outside surfaces of the main manifold 200 such that corresponding inlets and outlets of the modular components align with inlets and outlets of each of the outside surfaces of the main manifold 200. In the illustrated embodiments, the flame arrester module 110 (of
Internal conduits 204 of the main manifold 200 are machined or bored into the main manifold 200 from outside surfaces of the main manifold 200. Each of the internal conduits 204 connect the modular components to one another without the use of fittings, pipes or hoses, thereby reducing system complexity and reducing the risk of leak between fittings, pipes, hoses and other modular components. The internal conduits 204 are schematically illustrated in
The flame arrester module 110 is configured as a primary inlet and outlet for the measurement assembly 100 and in use protects the measurement assembly 100 from ignition of gaseous mixtures within the measurement assembly 100. The flame arrester module 110 includes an inlet 112 and an outlet 114. The inlet 112 and outlet 114 are connected to one or more flame arresters (118, 119) which prevent ignition of gaseous mixtures within the measurement assembly 100. In some embodiments, the input pressure of the fuel gas at the inlet 112 is within the range of 5 psi to 7 psi. In some embodiments, the output pressure of the fuel gas at the output 114 is at atmosphere (approximately 14.7 psi). In some embodiments, a plurality of flame arresters 119 are connected in parallel (indicated as parallel conduits 122) at arrester output 114. In some embodiments, three frame arresters 119 are connected in parallel at the outlet. 114. In some embodiments, an interface block 130 is positioned between the flame arrester module 110 and the main manifold 200.
Referring to
The main manifold 200 further includes a pressure sensor 212, a temperature sensor 214 and a variable pressure valve 216. In some embodiments, one or more of the pressure sensor 212, temperature sensor 214 and variable pressure valve 216 are internal to the main manifold 200. In some embodiments, one or more of the pressure sensor 212, temperature sensor 214 and variable pressure valve 216 are disposed within the thickness of the main manifold 200. In some embodiments, one or more of the pressure sensor 212, temperature sensor 214 and variable pressure valve 216 are modules external to the main manifold and are directly contacted to outside surfaces of the main module 200. The pressure sensor 212, temperature sensor 214 and variable pressure valve 216 receive the gaseous mixture from the measurement instrument module 160. The variable pressure valve 216 is configured to maintain and regulate the system pressure at a specific value. Thus, where fluctuations in pressure may occur due to a pump failure or a momentarily reduced pressure at the inlet 112, the variable pressure valve 216 will maintain the system pressure at the required level. As explained in further detail below, the redundant pump manifold assembly 300 is configured to periodically alternate operability between one or more pumps. During the operability transition between one or more pumps, the variable pressure valve 216 will maintain the system pressure at the required pressure level.
The redundant pump manifold assembly 300 includes a plurality of pumps (311, 312, 313) connected in parallel. The plurality of pumps (311, 312, 313) receive gaseous mixture from the variable pressure valve 216 and expel the gaseous mixture to the outlet 114 of the flame arrester module 110. In some embodiments, the redundant pump manifold assembly 300 further includes a 1-micron filter 302. Only one of the plurality of pumps (311, 312, 313) operate at a given time. In some embodiments, the redundant pump manifold assembly 300 includes three pumps (311, 312, 313). In some embodiments, the redundant pump manifold assembly 300 includes two pumps. In some embodiments, the redundant pump manifold assembly 300 includes four or more pumps.
A method 400 of operating the redundant pump manifold assembly 300 is illustrated in
The method 400 includes operating 410 a first pump 311 of the plurality of pumps for the operation period. After the end of the operation period of the first pump 311, the method 400 further includes validating 420 a second pump 312 of the plurality of pumps and, validating 430 a third pump 313 of the plurality of pumps. As used herein, the term “validating” shall mean performing a system check to determine if a pump of the plurality of pumps (311, 312, 313) is operational. In some embodiments, validating can include temporarily operating a pump of the plurality of pumps (311, 312, 313) for a validation time. In some embodiments, validating can include passing voltage through a pump of the plurality of pumps (311, 312, 313). In some embodiments, each pump the plurality of pumps (311, 312, 313) include a built-in validation feature known in the art. In some embodiments, the validation time is in the range of 1 second to 10 seconds. In some embodiments, system will wait for 10 seconds before evaluating if a pump of the plurality of pumps (311, 312, 313) is operating correctly. In some embodiments, to evaluate if a pump is operational, the system will determine if pressure in the cell is bellow a defined threshold. The system can further check by determining if a pump can maintain the pressure in the cell below a certain pressure (such as 202 hPa) for the validation time after the pump switch.
If the second pump 312 and the third pump 313 are operational, the method 400 further includes deactivating 442 the first pump 311 and operating 444 the third pump 313 for the operation period. The method steps 442 and 444 can be performed by the processor 502 as an if-then logic function 440 (illustrated in
If the second pump 312 is operational, but the third pump 313 is not operational, the method further includes deactivating 452 the first pump 311 and operating 454 the second pump 312 for the operation period. The method steps 452 and 454 can be performed by the processor 502 as an if-then logic function 450 (illustrated in
If the second pump 312 is not operational and the third pump 313 is not operational, the method 400 further includes operating 460 the first pump 313 continuously. In some embodiments, if one or all of the plurality of pumps (311, 312, 313) are not operational or otherwise defective, the processor 502 can send a warning to a user interface 506 (as shown in
The method 400 can be repeated. By way of example, after the third pump 313 has operated for the operation period, the method can further include validating the first pump 311, validating the second pump 312 and operating the second pump 312 for the operation period. After the second pump 312 has operated for the operation period, the method can further include validating the third pump 313, validating the first pump 311 and operating the first pump 311 for the operation period. Where one of the plurality of pumps (311, 312, 313) are not operational or are otherwise defective, the method 400 can perform continuous operation periods and validations for the remaining validated pumps. In some embodiments, the order of operation of the first, second and third does not reflect the only order of operation. The plurality of pumps (311, 312, 313) can be activated and shut down in any order and although the pumps are described as being shut down and activated singly, any number of pumps can be activated and shut down to maximize pump operability and minimize analysis cell down time.
The first plate 520 includes a first surface 522 and a second surface 524. The first surface 522 and the second surface 524 of the first plate 520 define a thickness T1 of the first plate 520. The second plate 550 includes a first surface 552 and a second surface 554. The first surface 552 and the second surface 554 of the second plate 550 define a thickness T2 of the second plate 550.
The first surface 522 of the first plate 520 is connected and abuts the fourth surface 210 of the main manifold 200 (of
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The systems and methods are not limited to the specific embodiments described herein but, rather, components of the systems and/or operations of the methods may be utilized independently and separately from other components and/or operations described herein. Further, the described components and/or operations may also be defined in, or used in combination with, other systems, methods, and/or devices, and are not limited to practice with only the systems described herein.
Although specific features of various embodiments of the invention may be shown in some drawings and not in others, this is for convenience only. In accordance with the principles of the invention, any feature of a drawing may be referenced and/or claimed in combination with any feature of any other drawing.
This written description uses examples to disclose the invention, including the best mode, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal language of the claims.