Patent Grant
11639824
The present disclosure relates to an apparatus and method for cooling a gas stream. Specifically, the apparatus and method involve a closed-circuit cooling liquid system for cooling a gas stream. More specifically, the closed-circuit cooling liquid system includes at least one heat exchanger in which a gas stream is cooled against a cooling liquid and at least one air cooler for cooling the cooling liquid after passing through the at least one heat exchanger. Also, the present disclosure describes a system including a compressor that compresses a gas stream that is cooled by the closed-circuit cooling liquid system.
In the discussion of the background that follows, reference is made to certain structures and/or methods. However, the following references should not be construed as an admission that these structures and/or methods constitute prior art. Applicant expressly reserves the right to demonstrate that such structures and/or methods do not qualify as prior art.
In many industrial processes, cooling of a gas stream is required. For example, in air separation units, gas is compressed in compressors and then cooled in compressor intercoolers. Compressor intercoolers are typically crossflow heat exchangers in which cooling liquid flows counter to the gas stream, such that heat from the gas stream passes to the cooling liquid. In turn, the cooling liquid increases in temperature and must be cooled prior to disposal or additional use in heat exchangers.
It is known to cool gas streams using cooling liquids. A typical method involves a heat exchanger in which a gas stream is cooled against a cooling liquid. Typically, water is used as a cooling liquid. Cooling water systems are typically designed as either single pass cooling water systems or open-circuit cooling water systems. Single pass cooling water systems are traditionally used for small plants that have minimal cooling demands due to the high water usage. Open-circuit cooling water systems are common for large plants and are comprised of a cooling tower which rejects heat to the atmosphere through evaporative cooling. However, in regions and climates which lack the water supply necessary to operate these systems, a closed-circuit cooling liquid system is employed. A closed-circuit cooling liquid system is comprised of an air-water heat exchanger where heat is rejected to the atmosphere through convection. In these systems, the return cooling liquid is pumped through exchanger tubes as heat is exchanged with air passing over the outside of the tubes. Air is forced through the exchanger using multiple fans in a forced or induced draft orientation.
Single pass cooling water systems require minimal capital cost but have larger cooling water demands and are not suited for large plants. The operating and capital costs of closed-circuit cooling liquid systems are typically much greater than that of the open-circuit cooling water system. This is due to the additional complexity of the air cooler and the lack of heat rejection through evaporation, resulting in larger equipment and greater footprint. Additionally, the lack of evaporative cooling requires additional air flow to provide the same cooling duty. This leads to significantly larger power consumption for a closed-circuit cooling liquid system.
In many cases, air flow for cooling the cooling liquid is provided via electrically driven fans. The increased power demand caused by such fans has a significant impact on the operational cost of the cooling system and overall plant.
Although there have been some attempts to find methods of designing closed-circuit cooling water systems, the overall cost and efficiency of the system has not been assessed. Many of the design parameters including air cooler layout, surface area, air flow, and footprint are adjusted to design the lowest cost solution for a given scenario. However, the adjustment of these parameters is completed independent of the design of the systems that utilize the cooling water. Accordingly, there remains a need for design schemes resulting in overall cost and efficiency gains in gas cooling systems.
It is desired to provide a process design scheme which uses a closed-circuit cooling liquid system and whose overall design leads to a lower operating power demand and lower capital cost. In general, this leads to a discharge temperature from the heat exchangers, such as intercoolers and aftercoolers, that is hotter than that recommended in the literature.
In the past, processes with a hot discharge temperature have resulted in excessive water loss, corrosion, and fouling in the exchangers, regardless of whether a closed-circuit or open-circuit system is used. The inventors have discovered that through an integrated design scheme, it is possible to reduce the energy required to operate the cooling system as well as reduce the overall cost of the total cooling system.
The present disclosure provides apparatus and method for cooling a gas stream utilizing a closed-circuit cooling liquid system designed in a manner that leads to a lower operating power demand and a lower capital cost. The present disclosure also provides a system for cooling a gas stream heated via a compressor that includes at least one compressor intercooler within a closed-circuit cooling liquid system.
One aspect of the described invention includes an apparatus including at least one heat exchanger in which a gas stream is cooled against a cooling liquid, whereby the cooling liquid temperature increases from a first temperature to a second temperature; at least one air cooler for cooling the cooling liquid after passing though the at least one heat exchanger, surface area of the at least one air cooler being designed to decrease temperature of the cooling liquid to the first temperature; a pump for circulating the cooling liquid; and conduits to form a closed-circuit for the cooling liquid to pass continuously through the at least one heat exchanger and the at least one air cooler. A ratio of surface area of the at least one air cooler to the surface area of the at least one heat exchanger is optionally 12 or lower.
In embodiments of the apparatus, the ratio is optionally 9 or lower, optionally 6 or lower, or optionally 3 or lower.
In embodiments of the apparatus, the surface area of the at least one heat exchanger and flow rate created by the pump is designed to result in a difference of temperature between the second temperature and first temperature being greater than 15° C. In other embodiments of the apparatus, the difference of temperature is at least 20° C., at least 25° C., or at least 30° C.
In embodiments of the apparatus, at least 2, at least 3, at least 5, at least 10, at least 15, at least 20 heat exchangers are used.
In embodiments of the apparatus, the at least one heat exchanger is a compressor intercooler or aftercooler.
A further aspect of the instantly described invention includes a method including providing at least one heat exchanger in which a gas stream is cooled against a cooling liquid, whereby the cooling liquid temperature increases from a first temperature to a second temperature; providing at least one air cooler for cooling the cooling liquid after passing though the at least one heat exchanger; providing a pump for circulating the cooling liquid; providing conduits to form a closed-circuit for the cooling liquid to pass continuously through the at least one heat exchanger and the at least one air cooler; pumping the cooling liquid through the closed-circuit at a flow rate that results in a difference of temperature between the second temperature and first temperature being greater than 15° C.; and powering the at least one air cooler to produce a cooling effect on the cooling water sufficient to decrease the temperature of the cooling liquid to the first temperature.
In embodiments of the method, the difference of temperature is at least 20° C., at least 25° C., or at least 30° C.
In embodiments of the method, a ratio of surface area of the at least one air cooler to the surface area of the at least one heat exchanger is optionally 12 or lower. In further embodiments, the ratio is optionally 9 or lower, optionally 6 or lower, or optionally 3 or lower.
In embodiments of the method, at least 2, at least 3, at least 5, at least 10, at least 15, at least 20 heat exchangers are used.
In embodiments of the method, the at least one heat exchanger is a compressor intercooler or aftercooler.
An aspect of the described invention includes a system including at least one compressor; at least one heat exchanger in which a gas stream compressed in the at least one compressor is cooled against a cooling liquid, whereby the cooling liquid temperature increases from a first temperature to a second temperature; at least one air cooler for cooling the cooling liquid after passing though the at least one heat exchanger, surface area of the at least one air cooler being designed to decrease the cooling liquid temperature to the first temperature; a pump for circulating the cooling liquid; and conduits to form a closed-circuit for the cooling liquid to pass continuously through the at least one heat exchanger and the at least one air cooler. A ratio of surface area of the at least one air cooler to the surface area of the at least one heat exchanger is optionally 12 or lower.
In embodiments of the apparatus, the ratio is optionally 9 or lower, optionally 6 or lower, or optionally 3 or lower.
In embodiments, the compressor compresses a gas in an air separation unit.
In embodiments of the apparatus, the surface area of the at least one heat exchanger and flow rate created by the pump is designed to result in a difference of temperature between the second temperature and first temperature being greater than 15° C. In other embodiments of the apparatus, the difference of temperature is at least 20° C., at least 25° C., or at least 30° C.
In embodiments of the apparatus, at least 2, at least 3, at least 5, at least 10, at least 15, at least 20 heat exchangers are used.
In embodiments of the apparatus, the at least one heat exchanger is a compressor intercooler or aftercooler.
The foregoing and other features of the invention and advantages of the present invention will become more apparent in light of the following detailed description of particular embodiments, as illustrated in the accompanying figures. As will be realized, the invention is capable of modifications in various respects, all without departing from the invention. Accordingly, the drawings and the description are to be regarded as illustrative in nature, and not as restrictive.
The apparatus and method of this invention will be described in detail with reference to the drawings.
Prior to describing the invention in further detail, the terms used in this application are defined as follows unless otherwise indicated.
The term “closed-circuit” refers to any combination of conduits and devices that results in a circuit in which all or substantially all fluid recirculates through the circuit.
The term “surface area of the at least one air cooler” refers to surface area of heat transfer between air and cooling liquid.
The term “surface area of the at least one heat exchanger” refers to the surface area of heat transfer between cooling liquid and gas stream
“Optional” or “optionally” means that the subsequently described circumstance may or may not occur, so that the description includes instances where the circumstance occurs and instances where it does not.
Before the present invention is described in greater detail, it is to be understood that this invention is not limited to particular embodiments described, as such may, of course, vary. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting, since the scope of the present invention will be limited only by the appended claims.
Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limit of that range and any other stated or intervening value in that stated range, is encompassed within the invention. The upper and lower limits of these smaller ranges may independently be included in the smaller ranges and are also encompassed within the invention, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included in the invention.
Certain ranges are presented herein with numerical values being preceded by the term “about.” The term “about” is used herein to provide literal support for the exact number that it precedes, as well as a number that is near to or approximately the number that the term precedes. In determining whether a number is near to or approximately a specifically recited number, the near or approximating unrecited number may be a number which, in the context in which it is presented, provides the substantial equivalent of the specifically recited number.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Although any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention, representative illustrative methods and materials are now described.
It is noted that, as used herein and in the appended claims, the singular forms “a”, “an”, and “the” include plural referents unless the context clearly dictates otherwise. It is further noted that the claims may be drafted to exclude any optional element. As such, this statement is intended to serve as antecedent basis for use of such exclusive terminology as “solely,” “only” and the like in connection with the recitation of claim elements, or use of a “negative” limitation.
As will be apparent to those of skill in the art upon reading this disclosure, each of the individual embodiments described and illustrated herein has discrete components and features which may be readily separated from or combined with the features of any of the other several embodiments without departing from the scope or spirit of the present invention. Any recited method can be carried out in the order of events recited or in any other order which is logically possible.
Disclosed is an apparatus including at least one heat exchanger in which a gas stream is cooled against a cooling liquid, whereby the cooling liquid temperature increases from a first temperature to a second temperature; at least one air cooler for cooling the cooling liquid after passing though the at least one heat exchanger, surface area of the at least one air cooler being designed to decrease temperature of the cooling liquid to the first temperature; a pump for circulating the cooling liquid; and conduits to form a closed-circuit for the cooling liquid to pass continuously through the at least one heat exchanger and the at least one air cooler. Also disclosed is a method in which the above apparatus is used. Further, disclosed is a system for using the above apparatus to cool a gas stream after the gas stream passes through at least one compressor.
An example of such a system including the above described apparatus is provided in
Referring to
A ratio of surface area of the at least one air cooler to the surface area of the at least one heat exchanger is optionally 12 or lower, optionally 9 or lower, optionally 6 or lower, or optionally 3 or lower.
Referring now to
Stream 102 is further compressed in compressor 1B to a higher pressure and is discharged at a higher pressure as stream 103. Stream 103 is cooled in process heat exchanger 2B against cooling water stream 200B, resulting in stream 104. Stream 104 may be used as a feed stream in, for example, an air separation unit. The heat of compression is transferred to the cooling water streams 200A and 200B, forming streams 201A and 201B, which combine to form stream 201 and flow to the closed-circuit cooling liquid air cooler 3.
The process heat exchangers 2A and 2B are designed in such a way as to minimize the temperature difference between streams 201A and 201B. The air cooler 3 rejects the heat of compression to the environment, lowering the temperature of the exiting cooling water to its initial value, stream 200.
The design of the integrated closed-circuit cooling system, however, is not limited to the exemplary design shown in
The integrated design of the closed-circuit cooling liquid system and the one or more process exchangers is derived from an analysis of the added cost of increasing or decreasing the size of the closed-circuit cooling liquid air cooler and the one or more process heat exchangers. The temperature difference of cooling water inlet stream 200 and outflowing stream 201, known as the cooling water temperature rise, is a major contribution to the advantage of the process. The cooling water temperature rise has an impact on both the design of the process heat exchanger and the closed-circuit cooling liquid air cooler. For example, a design with a low cooling water temperature rise will result in small process coolers and a large closed-circuit cooling liquid air cooler.
For designs according to this invention, the ratio of surface area of the at least one air cooler to the surface area of the at least one heat exchanger is optionally 12 or lower, optionally 9 or lower, optionally 6 or lower, or optionally 3 or lower.
A person of skill in the art is aware that there is a limit to the upper cooling water temperature, because running processes with a hot discharge temperature have resulted in excessive water loss, corrosion, and fouling in the exchangers. Generally, closed-circuit systems exhibit substantially less water loss and fouling in the exchangers. And although there is an upper temperature limit for the closed system where there will be excessive loss, corrosion, and fouling, that temperature is substantially higher than in an open system.
Open systems allow the water to pour down large open air cooling towers where air cools the water as it falls, generally resulting in large amounts of lost water, which must be added with every pass of water through the system. Each time additional water is added, new minerals and other contaminants are added to the system, increasing the total amount of mineral and contaminants in the system, which leads to corrosion and fouling, especially when water is heated to higher temperatures.
In contrast, while minerals and other contaminants may be present initially in the water in a closed circuit system, additional minerals and other contaminants do not further increase over time within such a system because additional water is not added. Accordingly, a higher temperature in the cooling water does not cause increased corrosion and fouling in a closed system in the same way as in an open system.
Modeling systems are based typically on open systems, and accordingly, the models discourage large cooling water temperature increases. However, the inventors discovered that within the closed systems described herein, substantially higher temperature increases can lead to substantial overall system cost savings, even when adding the cost and power consumption of air coolers.
It was found that the cooling water temperature rises in the process according to the invention can be as much as 30° C. or more, a rise not comprehended by modelling systems generally known to the person of skill in the art. As the cooling water temperature rise increases, the circulating water flow decreases resulting in reduced power usage and an increased size of the process heat exchangers or intercoolers. However, the air cooler exchanger size decreases due to the increased heat transfer driving force between the cooling water and the ambient temperature. The power usage of the closed-circuit cooling liquid to drive the fans is proportional to the system size, thus surprisingly resulting in reduced power usage.
But there is a practical limit to how high the cooling water temperature in the closed-circuit cooling liquid system can be. The process air cooler size increases exponentially as the outlet cooling water temperature begins to approach the inlet process temperature. As this occurs, the heat exchanger size becomes prohibitively large from increasing the cooling water temperature rise. Thus, the proposed design scheme is to integrate the design of the two systems to lead to an optimal power reduction given heat exchanger size constraints.
By way of an example of the invention, a simulation of the process depicted in
A large, multi-train air separation unit complex which produces >9,000 tons per day of oxygen has been designed using both a standard cooling water temperature rise of 14° C. and a cooling water temperature rise of, for example, 26° C. according to an embodiment of the invention. This results in a closed-circuit cooling liquid (CCCL) air cooler inlet temperature of 49° C. and 61° C. respectively. A plant of this size requires about 144 MW of cooling duty. The compressor intercooler/aftercooler exchangers and the air cooler are designed using the HTRI X-changer software suite. The example shows that the process according to an embodiment of the invention leads to an overall reduction in power of over 25% and a decrease in heat transfer surface area for the combined cooling system. The reduction in power is a result of the reduced water pumping and the reduction in the number of fan units in the closed-circuit cooling liquid air cooler unit from 72 fans to 56 fans. This reduction is achieved by increasing the driving force for heat transfer between the cooling water and the air. The results are summarized in Table 1.
Other ratios, less dependent on plant size, such as water flow rate, air cooler or exchanger surface area, and pump or fan power, each divided by total plant cooling duty (heat rejected to atmosphere) may prove useful as design tool and for comparison to conventional systems. For designs according to embodiments of this invention, the ratio of cooling water flow to cooling duty is less than 12 kg/MJ, or is less than 9 kg/MJ, and is more than 6 kg/MJ. In other embodiments, the ratio of air cooler surface area to cooling duty is less than 4500 m2/MW, or is less than 3500 m2/MW, and is more than 3000 m2/MW. In yet other embodiments, the ratio of intercooler or aftercooler exchanger surface area to cooling duty is more than 350 m2/MW, or is more than 600 m2/MW, and is less than 1300 m2/MW.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. It will be appreciated that the invention is not restricted to the details described above with reference to the preferred embodiments but that numerous modifications and variations can be made without departing from the spirit and scope of the invention as defined by the following claims.
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