The present invention is related to increasing the pressure of gas. Particularly, but not by way of limitation, a hydraulically driven positive displacement gas intensifier with provision of a lubrication system is presented.
After or in connection with purification of raw biogas to obtain biomethane, the gas is at least temporarily stored in compressed form. Compression is often the most costly step in biogas treatment, as commonly used compression equipment has high maintenance expenses and low durability.
Drawbacks of using e.g. existing hydraulic compressors for elevating the pressure of the target gas, such as the aforementioned biogas, include wearing of parts due to friction, a rise in temperature of the equipment, and formation of soot, which lead to a shortening of the operating life of the compressor among other potential side effects.
The objective is to present an intensifier with a lubrication system that will in addition provide cooling, which will at least reduce some of the problems stated above, and elongate the operating life compared to e.g. conventional dry-running hydraulic compressor types.
In accordance with one aspect of the present invention, a hydraulically driven intensifier for increasing pressure of gas comprises a hydraulically driven intensifier for increasing pressure of gas, said intensifier comprising a piston-driven compression chamber for gas, operatively connected to an adjacent hydraulic chamber further comprised in the intensifier, characterized by a lubricant coupling in the compression chamber of the compressor to circulate the lubricating fluid at least within an intermediate space, between the piston (or ram) and the hydraulic chamber, for cooling and lubricating the piston.
Having regard to the utility of various embodiments of the present invention, the provided lubrication system is economically executed, operates mechanically (automatically) and in a straightforward manner, thus making the system physically stable and easily maintained. The achieved effective circulation of lubricant provides for, besides lubrication of moving parts such as piston(s), specifically e.g. piston ring(s), within a compressor apparatus, also a desired cooling effect by transferring excessive heat away from the established hot spots such as the piston, which together increase both the life of the parts and the compressor in general. In preferred embodiments, the conduit through which lubricant is fed into the chamber has dimensions of such size that a substantial amount of lubricant may be circulated, which leads to a more prominent cooling effect than that of conventional lubrication systems. A substantial diameter of the conduit also leads to easy delivery of the lubricant into the chamber. For example, for a compression chamber for gas with a length of 600-700 mm and diameter of 100-150 mm, a lubricator conduit with a diameter of 0.5 inches is advantageously utilized. Field trials have shown that the operating life of the aforesaid piston rings may be in some embodiments extended up to several times (e.g. from about 1000 h to about 7000 h) by the present solution. A further benefit of various embodiments of the present invention is given by potential reduction of soot etc. formation or elimination thereof.
In addition to being affordable and robust, the arrangement is readily scalable, as several intensifiers may be used, conducting the discharged gas to the suction inlet of another compression chamber to achieve a desired compression ratio, thus constituting a multistage compression system. One unit may be single- or multi-acting, i.e., have one or more compression chambers. Multistage compression may also be achieved in one intensifier, where gas compressed in one compression chamber is directed into another compression chamber with smaller volume in the same multi-acting intensifier. The enabled intensifier configurations can achieve an effective compression ratio, and depending on the embodiment, the arrangements may be portable.
In some use scenarios, an embodiment of the present invention may be adopted as a part of a more comprehensive process involving e.g. the use of chemical or other type of reactor. An intensifier according to the present invention may, however, be used to increase the pressure of any gas.
The present invention will be described in greater detail with reference to the accompanying drawings, in which:
The term “intensifier unit” refers hereafter to an intensifier device which comprises one (common) body of preferably rigid type. In some embodiments, the body may be of substantially monolithic nature defined by a single element or several permanently attached elements. In some other embodiments the body may comprise multiple functional elements such as chambers removably connected together by necessary fixing elements such as bolts.
In the shown embodiment, a single-stage double-acting intensifier unit is presented, but the fundamental principle of the invention may be utilized in a multi-stage intensifier unit. A single-acting intensifier unit is also feasible according to the present invention.
The intensifier (unit) 100 of
In the embodiment of
The gas chambers may be separated from the hydraulic chamber by suitable separating elements 136 and 138 which may comprise one or more parts, such as a hydraulic connection rod seal assembly and a connection block or flange or other such suitable structures.
The hydraulic chamber 104 comprises inlets/outlets 116, 122 (whose inlet/outlet roles may change dynamically depending on the current working direction of the piston 110 as being easily appreciated by a person skilled in the art) for hydraulic fluid flow. In some embodiments the chamber, piston, rod, pipe(/tube/conduit), and/or separating element materials may generally include e.g. metal, alloy, cast iron, plastics, steel, stainless steel, aluminum, brass, bronze, ceramics, and/or nickel-alloy.
From a functional point of view, gas is brought into the first gas chamber 102 through an inlet 118, which permits flow into the chamber, while compressed gas exits the gas chamber 102 through the outlet 120, which permits flow out of the chamber 102. The second gas chamber 106 may have a substantially similar configuration with the inlet 130 and outlet 128.
Compression of gas in the chamber 102 is effectuated through the flow of hydraulic fluid. Hydraulic fluid that is conducted into the hydraulic chamber 104 via the inlet 116 causes the piston 110 to move, which, through the connecting rod 114, causes the fluid piston 108 to move, thereby compressing the gas in the gas chamber 102.
The compressed gas exits the chamber 102 via the outlet 120 and the direction of flow of the hydraulic fluid is reversed, allowing uncompressed gas to be recurrently conducted into the gas chamber via the inlet 118.
The work cycle in the chamber 106, which in the embodiment of
In a multi-acting intensifier unit, the alternating direction of flow of the hydraulic fluid thus determines in which gas chamber 102, 106 the compression takes place.
In terms of lubrication, in various embodiments the lubricating fluid may be fed into the first gas chamber 102 through the inlet 124, situated e.g. next to the separating element 136, and exit the chamber 102 through the outlet 126, a similar arrangement being generally suitable also for the second gas chamber 106, with corresponding inlet 132, outlet 134, and separating element 138.
An embodiment of the flow of fluids to and from the first gas chamber 102 and the hydraulic chamber 104 of the intensifier of
In this embodiment, gas not yet compressed by the intensifier 100 is conducted from a storage unit 202 into the intermediate space (volume) 102a, residing between the gas inlet 118 or outlet 120 and the fluid piston 108 within a gas chamber 102. After compression, the gas travels through the outlet 120 into a storage unit 204 intended for the compressed gas.
The hydraulic fluid that drives the compression is conducted to and from the hydraulic chamber 104 through the inlet and outlet 116 or 122, respectively. The fluid may be supplied from the hydraulic fluid reservoir 206, into which it may also be returned. The hydraulic fluid may, for instance, be hydraulic oil or other fluid that is suitable for the application.
In one embodiment, as the piston 108 is being driven to compress the gas by decreasing the volume 102a, the volume of the substantially neighboring space 102b, located between the piston 108 and the separating element 136, increases, leading to the formation of a vacuum or generally a space of lower pressure in contrast to the environment including the inlet 124 and/or reservoir 208, which will cause or at least facilitate lubrication fluid to flow into the space 102b through the inlet 124 and/or at least spread therein. A similar setup may be employed in the second gas chamber 106.
In the embodiment of
In alternative or supplementary embodiments, at least one drive entity 210 may be employed, comprising one or more elements such as pumps for circulating the hydraulic fluid and/or lubricant. E.g. electric motor(s) may be utilized to drive the pump(s) or other circulation-enhancing mechanism of the hydraulic and/or lubricating fluid.
The lubrication fluid, typically essentially liquid, may in various embodiments optionally be the same fluid that is used as hydraulic fluid, e.g. oil. Alternatively, different lubrication fluid such as different oil may be utilized.
In the embodiment of
Two or more intensifier units 100 may be coupled to implement a multistage compression system. In
Number | Date | Country | Kind |
---|---|---|---|
20165757 | Oct 2016 | FI | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/FI2017/050706 | 10/6/2017 | WO | 00 |