WO2021061431A1

WO2021061431A1 - Manufacturable metal-graphene interface for highly efficient and durable heat exchanger components

Info

Publication number: WO2021061431A1
Application number: PCT/US2020/050688
Authority: WO
Inventors: Chen Li; Wei Chang; Benli Peng; Pengtao Wang
Original assignee: University Of South Carolina
Priority date: 2019-09-24
Filing date: 2020-09-14
Publication date: 2021-04-01

Abstract

The present disclosure relates to efficient heat exchanger components such as pipes, as well as apparatuses including the same. Methods of fabricating heat exchange components are also disclosed. An example heat exchanger component can include a condenser surface having a substrate and one or more layers of graphene. The substrate can be formed of nickel and a nickel-graphene surface composite layer can be formed. The substrate-graphene composite can be highly durable, hydrophobic, and resistant to fouling. Example implementations may also demonstrate dropwise condensation.

Description

MANUFACTURABLE METAL-GRAPHENE INTERFACE FOR HIGHLY EFFICIENT AND DURABLE HEAT EXCHANGER COMPONENTS

GOVERNMENT SUPPORT

[0001] The subject invention was made with government support under a research project supported by the National Science Foundation, Grant No. 1357920. The government has certain rights in the invention.

PRIORITY INFORMATION

[0002] The present application is an international application which claims priority to U.S. Patent Application Serial No. 16/580,249, filed on September 24, 2019, which is a continuation in part of U.S. Patent Application Serial No. 16/217,100, filed on December 12, 2018, which claims priority to U.S. Provisional Patent Application Serial No. 62/607,154, filed on December 18, 2017, the entire disclosures of which are incorporated by reference herein.

BACKGROUND

[0003] Heat exchanger components, such as condensers, are important to many industries. For example, condensers are widely used in the petrochemical industry, as well as for water purification, desalination, and power generation. In power generation, steam is made from heat generated by fossil fuels or other sources. The steam generation creates high pressures and the steam flows through a turbine to a lower pressure area and eventually collects as water on a condenser. Therefore, the condenser creates a low-pressure environment by removing steam from the system and producing water. Unfortunately, according to some estimates, condenser inefficiencies result in 50% or more wasted energy. [0004] Condenser inefficiency can occur for a variety of reasons. Regardless of the cause, the problem is inefficient heat transfer across the condensing elements. One cause of inefficiency is simply the buildup of a layer of water on the surface of the condenser, which acts as an insulating element. This phenomenon is what is known as film-wise condensation (FWC), in which the insulating blanket of water slows heat transfer from the coolant side to the steam condensing side. Researchers have attempted to mitigate this problem by adopting dropwise condensation (DWC) using hydrophobic surfaces. In dropwise condensation, drops of water form on the condenser surface and are quickly carried away under their own weight or by another mechanism. This avoids the formation of the film of water that acts as an insulator. However, hydrophobic materials tend to be poor heat conductors and the efficiency gains made by adopting hydrophobic materials are negated by their reduced heat transfer ability.

[0005] Other attempts to adopt DWC include applying thin layers of hydrophobic materials, such as polymer coatings, on condenser surfaces. However, most coatings tend to deteriorate quickly as they are not well suited for long-term operation in corrosive environments with high temperatures and steam. Scale buildup and biofouling have also proven to be a significant source of condenser inefficiencies. The scale and biofilms formed on the surface of the condenser can also act as an insulating layer that prevents heat transfer. Condenser biofouling and scale buildup may be especially prevalent in water desalination and purification. To prevent biofouling and scale buildup, chemical treatment, such as chlorination, is often used. Of course, biofouling, scale buildup, and even the chemical treatment used to prevent these issues are detrimental to thin, hydrophobic condenser coatings, and further complicate the goal of achieving efficient heat transfer and dropwise condensation.

[0006] Heat exchanger efficiency is an important objective for both industrial and domestic applications. The seemingly simplistic nature of condenser function is deceiving as improving condenser efficiency in practice is a complicated problem that presents multiple challenges. Accordingly, the art is in need of new technologies for increasing condenser efficiency, increasing condenser durability, and promoting dropwise condensation.

BRIEF SUMMARY

[0007] The present disclosure relates to efficient heat exchanger components and apparatuses including the same. Methods of fabricating heat exchanger components and, specifically, component surfaces, are also disclosed. According to an example embodiment, a heat exchange apparatus in accordance with the disclosure can include one or more tubes for flowing a coolant through the interior of the tubes to condense a transfer fluid such as water vapor. At least one of the one or more tubes can include a coating on the condenser surface (i.e., the surface that is not in contact with the coolant). In general, the coating can include a metal (e.g., nickel), a carbon material (e.g., graphene), or a combination thereof (e.g., the metal coating applied to the exterior surface and the carbon material deposited on the metal coating). Using a combination can produce unexpected advantages such as improving corrosion resistance and/or heat transfer efficiency.

[0008] An embodiment includes a heat exchanger component having a transfer side and a condensing side. A substrate to receive the graphene can be formed on the transfer side, the condensing side, or both the condensing side and the coolant side. In general, the graphene can be applied to the substrate in a single layer or in multiple layers (e.g., 1-30 layers), each having layer thickness. The substrate can be a metal substrate made of materials such as nickel, nickel alloys, copper, or copper alloys.

[0009] The graphene layers may be viewed as a coating but may be better described as an integrated composite material with the substrate. Specifically, p-orbitals of the graphene can hybridize with the d-electrons of the substrate. This electron hybridization can be particularly effective with nickel and nickel alloys and can result in robust surface properties that are resistant to corrosion, biofouling, and chemical attack. Furthermore, the graphene- functionalized substrate can maintain a hydrophobic surface and allow for efficient dropwise condensation (DWC).

[0010] The thermal expansion mismatch between the substrate and the graphene can be minimized to prevent the graphene layers from detaching from the substrate surface. In some embodiments, the thermal mismatch is less than 25 x 10⁶k ¹ , and, in some embodiments, can be less than 18 x lO^k ¹. Graphene can be applied to the substrate in various ways. For example, graphene can be applied to the substrate using chemical vapor deposition (CVD), thin film physical vapor deposition (PVD) such as direct current magnetron sputtering, or deposition of hydrogenated amorphous carbon. In one particular embodiment, the graphene can be applied via atmospheric pressure chemical vapor deposition (APCVD).

[0011] The graphene layer can have a thickness from 1.0 nm to 100 nm, or greater. The substrate can be fabricated from brass, copper, nickel, aluminum, stainless steel, carbon steel, or a mixture or alloy of any of the previous compositions.

[0012] In general, the present disclosure provides examples demonstrating improved condensation efficiency, as well as durability (e g., corrosion resistance), that may benefit certain applications by improving energy efficiency and reducing maintenance costs.

BRIEF DESCRIPTION OF THE DRAWINGS [0013] A full and enabling disclosure of the present invention, including the best mode thereof to one skilled in the art, is set forth more particularly in the remainder of the specification, which includes reference to the accompanying Figures, in which:

[0014] FIG. 1 shows a nickel -graphene interface according to an embodiment of the present invention.

[0015] FIG. 2 shows a scanning electron microscope image of graphene layers on a nickel substrate. [0016] FIG. 3 shows DWC occurring on a tube with a nickel -graphene surface.

[0017] FIG. 4(a) shows a Raman spectroscopy graph for multiple layers of graphene on a nickel tube

[0018] FIG. 4(b) shows heat transfer coefficients (HTCs) of a pure nickel tube and a nickel tube having graphene layers according to an embodiment; FIG. 4(c) shows HTCs after a period of 33 days.

[0019] FIG. 5(a) shows an X-ray photoelectron spectroscopy (XPS) graph of the peak intensity of a copper-graphene interface after a two-hour test.

[0020] FIGs. 5(b), 5(c), and 5(d) show the peak intensity of nickel-graphene interfaces after a one-month test.

[0021] FIGs. 6(a), 6(b), and 6(c) show efficient DWC and HTCs of nickel-graphene surfaces.

[0022] FIG. 7(a) shows the corrosion rate of copper-graphene interfaces.

[0023] FIG. 7(b) shows the corrosion rate of nickel -graphene interfaces.

[0024] FIG. 8 shows a heat exchanger wall having substrate-graphene interfaces on both a coolant side and a condenser side.

[0025] FIGs. 9(a) and 9(b) show microcopy images of the surface of an example heat exchanger component according to the present disclosure.

[0026] FIG. 9(c) shows a 3-dimensional representation of the surface of an example heat exchanger component according to the present disclosure.

[0027] FIG. 10(a) and shows a graph displaying example data for heat flux versus DT using the comparative examples: pure Ni and Ni-G.

[0028] FIG. 10(b) compares the same example data in FIG. 10(a) to example data from a heat exchange component according to the present disclosure: Cu-Ni-G with NCG.

[0029] FIG. 11 shows a graph displaying example data for heat flux versus DT using an example embodiment of the disclosure measured at 1, 2, 3, 7, 14, or 30 days. Also displayed is a comparative example: pure Ni.

[0030] FIGs. 12(a)- 12(1) show images taken of dropwise condensation occurring on a heat exchanger component. FIGs. 12(a)- 12(d) display images of an example embodiment in accordance with the disclosure. FIGs. 12(e)- 12(h) and FIGs. 12(i) to 12(1) illustrates images of comparative examples.

[0031] FIG. 12(m) shows an image taken of DWC for an example embodiment in accordance with the disclosure after 90 days. [0032] FIGs. 13(a)- 13(c) show graphs comparing example data taken from example embodiments of the disclosure (Cu-Ni-G) to data from comparative examples (Cu, Cu-Ni and Ni-G).

[0033] Repeat use of reference characters in the present specification and drawings is intended to represent the same or analogous features or elements of the present invention.

DETAILED DESCRIPTION

[0034] Reference now will be made to the embodiments of the invention, one or more examples of which are set forth below. Each example is provided by way of an explanation of the invention, not as a limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations can be made in the invention without departing from the scope or spirit of the invention. For instance, features illustrated or described as one embodiment can be used on another embodiment to yield still a further embodiment. Thus, it is intended that the present invention cover such modifications and variations as come within the scope of the appended claims and their equivalents. It is to be understood by one of ordinary skill in the art that the present discussion is a description of exemplary embodiments only and is not intended as limiting the broader aspects of the present invention, which broader aspects are embodied exemplary constructions.

[0035] The present disclosure relates to efficient and robust heat exchanger components, apparatuses including said components, and fabrication methods thereof. Heat exchangers play an important role in many industries including petrochemicals, automotive, heating ventilation and air conditioning (HVAC), power generation, and water purification and desalination.

[0036] An example implementation of the present disclosure includes a heat exchanger component that comprises a condenser surface (e.g., the surface in communication with a working fluid such as a coolant) and a transfer surface (e.g., the surface in communication with a transfer fluid such as steam or other condensable gases). Together, the condenser surface and the transfer surface define a continuous region, such as a pipe, that can be made from a substrate material. A coating can then be applied to the substrate such that the coating directly touches or is bound to the substrate. This coating can be applied to at least the condenser surface, though in some implementations, the coating may be applied to the condenser surface and the transfer surface. Generally, the coating can include a layer material that can include a metal (e.g., Ni), a carbon material (e.g., graphene), or the metal and the carbon material (e.g., the carbon material deposited on the metal, deposited on the substrate). [0037] While the transfer fluid is generally exemplified throughout the disclosure as steam, other transfer fluids can be used in heat exchangers that incorporate components according to the present disclosure For instance, promising results have also been shown for polar, non-ionizing (under standard conditions) solvents such as ethanol, acetone, tetrahydrofuran, etc., in addition to water. Further, in certain implementations, the transfer fluid may include a mixture of fluids. Thus, implementations of the disclosure may demonstrate similar advantages for applications such as refrigeration and need not be limited to only steam condensation.

[0038] Several non-limiting examples of heat exchanger components can include pipes which have a structure that allows flowing a coolant along a direction to induce condensation. Also included are heat pipes which are generally closed structures that include a heat transfer surface and a condensation surface.

[0039] Methods of fabricating condensers, and specifically, condenser surfaces, are also disclosed. FIG. 1 shows a condenser surface 100 according to an embodiment of the present invention. The condenser surface includes of a substrate 101 and one or more layers of graphene 102. One, two, three, or more layers of graphene 102 can be formed on the substrate. The graphene can be formed as a layer on the substrate but may preferably be formed in a manner that results in the creation of a substrate-graphene composite in which the graphene is integrated with the substrate material. That is, the molecular structure of the graphene can interact and even embed itself within the molecular structure or crystal lattice of substrate. Specifically, p-orbitals of the graphene can hybridize with the d-electrons of the substrate. The unique nature of the nickel -graphene composite allows for especially strong bonding. For example, the separation between the graphene and the substrate can be from about 0.05 nm to about 0.5 nm, preferably from about 0.1 nm to about 0.3 nm, and even more preferably from about 0.15 nm to about 0.25 nm. In a specific example, the separation between the respective materials in nickel -graphene composites is approximately 0.21 nm. [0040] The substrate 101 can be formed of any material that is conventionally known in the art including stainless steel, copper, brass, nickel, aluminum, titanium, as well as mixtures and alloys thereof. In some embodiments, the thermal mismatch between the graphene layers and the substrate can be less than 25 x 10 ¾^_1, such as less than 20 x 10 ¾^_1, such as less than 18 x 10⁶k l, such as less than 15 x 10 ^f>k ¹. The thermal mismatch can also range from about 25 x 10⁶k l to about 8 x 10⁶k ¹. such as from about 19 x 10 k ¹ to about 11 x 10 A ¹, such as from about 16 x 10⁶k l to about 12 x 10⁶k ¹. [0041] In a specific embodiment, the substrate 101 can be a nickel or nickel alloy. Nickel and nickel alloys have been found to work particularly well with graphene, and it is believed that the graphene embeds itself within, or binds tightly with, the crystal lattice of the nickel substrate. The condenser can also be formed of a base material (such as stainless steel, copper, brass, aluminum, titanium, as well as mixtures and alloys thereof) that acts as the structural support of the condenser with a thin layer of nickel or nickel-alloy present on the surface of the base material. The thin layer of nickel or nickel-alloy on the surface of the base material can be applied using, for example, electroplating techniques. The nickel or nickel- alloy coating can therefore have a thickness of from about 1 to about 100 micrometers, such as from about 20 to about 80 micrometers, such as from about 40 to about 60 micrometers. [0042] FIG. 2 shows a scanning electron microscope image of graphene layers on a nickel substrate. The image shows a relatively uniform and defect-free graphene structure. The graphene grain sizes should optimally be large and defect-free and can have an average diameter or width of greater than about 3 micrometers, such as greater than about 5 micrometers, such as greater than about 10 micrometers, such as greater than about 20 micrometers. Furthermore, the graphene grain sizes (or diameter, or width) can range from about 1 micrometer to about 50 micrometers, such as from about 3 micrometers to about 30 micrometers, such as from about 10 micrometers to about 20 micrometers.

[0043] FIG. 3 shows a tube condenser having a nickel-graphene composite surface in accordance with an embodiment of the present disclosure. The tube condenser of FIG. 3 has coolant running within the tube and steam condensing on the surface of the tube. Dropwise condensation is achieved on the surface of the tube. The dropwise condensation wipes away water films from the surface of the tube and keeps water films from forming an insulating layer that would reduce the heat transfer of the condenser. The dropwise condensation is achievable due to the hydrophobic nature of the nickel -graphene composite surface. The hydrophobic surface may be attributable to weak van der Waals forces between the graphene layers and the out-of-plane water droplets. This may result in reduced drag forces between the substrate-graphene surface and the water droplets and further promote dropwise condensation.

[0044] The substrate-graphene surface can be applied to any conventional condenser material which acts as a structural base and provides structural integrity. For example, the base of the condenser can be made of conventional materials that are known in the art, such as stainless steel, carbon steel, titanium, aluminum, copper, nickel, brass, and mixtures and alloys, therefore. The base can form the structural support for condenser tubing and fins that promote heat transfer. The substrate can then be applied to the condenser base followed by the layers of graphene. Alternatively, the condenser base can serve directly as the substrate. [0045] FIG. 8 shows a heat exchanger wall 800 having substrate-graphene interfaces on both a coolant side 801 and a condenser side 802. The heater exchanger wall 800 can have a base material 803 that serves as a structural support. A substrate layer 804 can be formed on one or both sides of the heat exchanger wall 800. One or more layers of graphene 805 can be applied to the substrates 804, or a suitable base material 803 can directly serve as the substrate.

[0046] Graphene can be applied to the substrate in various ways. For example, graphene can be applied to the substrate using chemical vapor deposition (CVD), atmospheric pressure CVD, thin film physical vapor deposition (PVD) such as direct current magnetron sputtering, and deposition of hydrogenated amorphous carbon. The graphene layer can have a thickness greater than about 5 nm, such as greater than about 10 nm, such as greater than about 20 nm, such as greater than about 30 nm. The graphene layer’s thickness can also range from about 2 nm to about 100 nm, such as from about 5 nm to about 50 nm, such as from about 10 nm to about 30 nm.

[0047] Graphene composite interfaces of the present disclosure can reduce biofouling by reducing bacterial adhesion by 50% or more. Calcium sulfate and other scale deposition rates can also be reduced. Furthermore, low surface energy graphene interfaces can be easily cleaned to remove scale and biofouling agents as their contact adhesion force is lessened by the graphene composite surface.

[0048] The present invention may be better understood with reference to the following examples.

Example 1

[0049] Nickel-graphene composite surfaces were produced. FIG. 4(a) shows a Raman spectroscopy graph for one, two, and three layers of graphene on a nickel substrate. FIG. 4(b) shows heat transfer coefficients (HTCs) of a pure nickel tube and a nickel tube having graphene layers. The nickel -graphene surface is able to produce approximately 150% greater heat transfer than the nickel tube without graphene. FIG. 4(c) shows HTCs after a period of 33 days. It shows that the nickel -graphene composite surface maintained superior heat transfer over the nickel only surface.

Example 2

[0050] Both copper-graphene-monolayer and nickel-graphene-multilayer interfaces were prepared for steam condensation testing. Both surfaces were examined by X-ray photoelectron spectroscopy (XPS) before and after condensation experiments. As illustrated by FIG. 5(a), copper-graphene was oxidized after one two-hour test and quickly lost its graphene enhancement. In contrast, after a month-long test in air, the nickel-graphene composite did not show much oxidation, as seen in FIGs. 5(b), 5(c), and 5(d). The slight degradation in HTCs is likely due to the accumulation of hydroxyl groups (FIG. 5(b)), which increased with test time (FIG. 5(c)). This study shows that nickel -graphene interfaces exhibit superior anticorrosion properties in harsh steam environments. The superior durability of the nickel-graphene interface could be due to the similarities in thermal expansion between nickel and graphene. The thermal expansion mismatch between the graphene monolayer and the copper substrate is on the order of 19.2* lO^K ¹, causing the graphene to separate from the copper substrate. However, the nickel-graphene interface has a smaller thermal expansion mismatch, on the order of 14x 10⁶K ^L. Considering the additional lubrication effect between graphene layers, the nickel -graphene interface showed far better thermal expansion mismatch and durability. [0051] FIGs. 6(a), 6(b), and 6(c) show efficient DWC and HTCs of nickel-graphene surfaces. As illustrated in FIG. 6(a), nickel -graphene interfaces can enable up to six-times greater heat flux compared to other condenser surfaces. FIG. 6(b) shows equally important that, even with a high percentage of air, an approximately 180% enhancement is still achieved by a nickel -graphene interface relative to the state-of-practice FWC. HTCs generally decrease with lower working pressure, but the nickel -graphene interfaces still showed significant enhancement of approximately 200% at 0.4 atmospheres of pressure and at a subcooled temperature of 10°C. FIG. 6(c) shows HTCs with different steam pressures. FIG. 6(c) demonstrates that higher steam pressures produce greater HTCs. However, all of the HTCs demonstrated are greater than the film-wise HTCs, as shown in the shaded lower portion.

Example 3

[0052] Corrosion studies were performed using Tafel analysis. FIG. 7(a) shows the corrosion rates of copper-graphene interfaces and FIG. 7(b) shows the corrosion rates of nickel-graphene interfaces. As illustrated in FIG. 7(a), copper-graphene initially shows a low corrosion rate. However, once corrosion starts to occur locally, the corrosion rate begins to accelerate rapidly and globally. In contrast, and as illustrated in FIG. 7(b), the nickel- graphene interface is extremely stable and showed an approximately 450x lower corrosion rate even after a fourth test.

[0053] These and other modifications and variations to the present invention may be practiced by those of ordinary skill in the art, without departing from the spirit and scope of the present invention, which is more particularly set forth in the appended claims. In addition, it should be understood the aspects of the various embodiments may be interchanged both in whole or in part. Furthermore, those of ordinary skill in the art will appreciate that the foregoing description is by way of example only and is not intended to limit the invention so further described in the appended claims.

Example 4

[0054] Microscopy images where taken of a heat exchanger component using a scanning electron microscope (SEM) or atomic force microscope (AFM). In FIGs. 9(a)-9(c), different images are shown of graphene coated Ni/Cu. In FIG. 9(a), an image of the top surface of graphene coated Ni/Cu is displayed along with an insert displaying the hydrophobicity as illustrated by the contact angle of a water droplet placed on the surface. In FIG. 9(b), a cross- section of graphene coated Ni/Cu is shown along with imagery indicating the copper (Cu) substrate having a nickel (Ni) coating. Layers of graphene are thin and cannot readily be distinguished from Ni coating that the graphene layers are deposited above. FIG. 9(c) illustrates an AFM image displaying surface morphology of graphene coated Ni/Cu.

Example 5

[0055] FIGs. 10(a), 10(b), and 11 show images of heat flux data at a given temperature difference (DT). FIG. 10(a) displays data for materials including graphene coated Ni/Cu (Cu- Ni-G), graphene coated nickel (Ni-G), and nickel (Ni). FIG. 10(b) shows an image of heat flux data at a given DT for the same materials in FIG. 10(a) in the presence of a non condensable gas (NCG). In FIG. 11, performance durability is illustrated by comparison of an example material made of Cu-Ni-G that has been used for 1-30 days to pure nickel. Conditions for the durability test included in some cases one or more open loop steam condensation cycles. In an example procedure for the durability test, Ni/G, Cu/G and Cu/SAM tubes having about 6.35 mm diameter and about 92mm effective condensation length were used to conduct the open loop condensation test for durability evaluation.

[0056] Non-condensable gases (NCG) were calculated indirectly by comparing the chamber pressure (Pi) measured by the pressure transducer to that pressure computed by the measurement of the saturated temperature (T2) using the thermocouple inside the chamber (P2). The saturated water vapor pressure was calculated based on the Goff-Gratch equation which is a function of saturated temperature:

During a typical open loop condensation experiment, the percentage of NCG ranged between about 2.2% and 5.6%. In general, the maximum percentage of NCG was observed at the very beginning of the experiment where higher subcooling temperature was achieved. With the increase of experimental time, the NCG inside the chamber turned out to be reduced due to the continuous supplement of steam. When performing multiple condensation cycles, during the first 2 weeks, one open loop condensation test was conducted and then exposed in air for the next test cycle on each day. During the period of 2-4 weeks, 5-13 weeks, 13-24 weeks and 24-60 weeks, tests were conducted every 2 days, 7 days, 14 days and 30 days respectively. After 60 weeks of thermal cycle test, the frequency was kept to 1/30 to evaluate the air exposure effect on the surface stability.

Example 6

[0057] FIGs. 12(a)-12(m) illustrate a time course of images displaying DWC under atmospheric pressure in the presence of a NCG using the materials: Cu-Ni-G, Ni-G, and surface assembled monolayer copper (Cu-SAM).

Example 7

[0058] FIGs. 13(a)-13(c) display data representative of corrosion resistance for Cu, Cu- Ni, Cu-Ni-G, and Ni-G. In FIG. 13(a), Tafel plots are illustrated for Cu, Cu-Ni alloy, Cu-Ni- G, and Ni-G samples. Best fittings for corrosion current are represented by the dash lines. In FIG. 13(b), corrosion rates are shown for the Cu, Cu-Ni alloy, Cu-Ni-G, andNi/G samples based on data extracted from the Tafel plots. In FIG. 13(c), the corrosion rate of cumulated Tafel test is displayed on the same Cu, Cu-Ni alloy, Cu-Ni-G, and Ni/G samples.

Example 8

[0059] Methods for electroplating substrate surfaces were conducted using the following procedure. As an example, a pure copper plate (-99.5%, thickness 0.125 mm, McMaster-Carr^® Supply Co.) and tube (-99.5%, OD=6.35 mm and ID=4.57 mm, McMaster-Carr^® Supply Co.) were used for surface characterization and a steam condensation test on nickel plating sample surfaces, respectively. Before the electroplating, all copper surfaces were first immersed in a 5% sulfuric acid for 10 minutes to remove the native oxide layer, then rinsed with DI water. The sample surfaces were then immersed in an acetone and ethanol bath separately for ultrasonic cleaning for 5 minutes each to clean up possible organic contaminations, and then rinsed by DI water three times followed with nitrogen gun blown to dry. Then a thin layer nickel (-2.1 pm) was deposited on these copper sample surfaces by using commercial electroplating electrolyte (Techni Nickel S solution from Technic Inc.). The electrolyte temperature was controlled to be 54 °C by a water bath for an optimized reaction temperature. The current density was controlled to be 0.3 ASD and the electroplating time was set to 10 minutes. Hence, the graphene growth was successfully demonstrated on thin nickel films with a thickness of 200-300 nm; the thickness of nickel layer for subsequent graphene growth could be set, which was more than 300 nm. Considering the graphene growth condition and the potential nickel-copper interdiffusion which could benefit the anticorrosion of sample surfaces, we set the thickness of this thin nickel coating to be ~2.1 pm for reproducible and uniform graphene coating growth.

[0060] For graphene growth on these nickel-plated copper surfaces, atmospheric pressure chemical vapor deposition (APCVD) process was conducted in a quartz tube (OD=l”) equipped with a horizontal tube furnace (Lindberg/Blue M^™, ThermoFisher^™). Samples were then heated up to 1000 °C with argon and hydrogen gas (500/200 seem) flowing over the sample prior to graphene growth. Methane gas (20 seem) was introduced while keeping the argon and hydrogen gas supply for over 20 minutes to get full coverage of graphene coating on the sample surface. The samples were cooled down to room temperature by fast cooling (at a cooling rate of 100 °C/min) while keeping the same gas flow.

Claims

WHAT IS CLAIMED IS:

1. A heat exchange component comprising: a condenser surface in communication with a working fluid; and a transfer surface in communication with a transfer fluid, wherein the condenser surface and the transfer surface define a continuous region comprising a substrate having a coating deposited on at least the condenser surface, and wherein, the coating comprises a metal, a carbon material, or the carbon material deposited on the metal.

2. The component of claim 1, wherein the continuous region defines a pipe.

3. The component of claim 1, wherein the continuous region defines a heat pipe.

4. The component of any one of the preceding claims, wherein the substrate comprises copper.

5. The component of any one of the preceding claims, wherein the coating comprises nickel or a nickel alloy.

6. The component of any one of the preceding claims, wherein the carbon material comprises graphene.

7. The component of claim 6, wherein the graphene is deposited as one or more layers.

8. The component of any one of the preceding claims, wherein the coating comprises nickel or a nickel alloy and wherein the nickel or nickel alloy further comprises graphene deposited on the nickel or nickel alloy.

9. The component of claim 8, wherein the nickel has a coating thickness of less than about 2 micron.

10. The component of claim 8 or 9, wherein the graphene has a thickness of about 1.0 nm to about 10.0 nm.

11. A heat exchange apparatus comprising two or more of the heat exchange components of claim 1.

12. The heat exchange apparatus of claim 11, wherein the apparatus comprises a plurality of pipes and wherein each pipe included in the plurality of pipes comprises copper having nickel deposited on the condenser surface.

13. The heat exchange apparatus of claim 12, wherein each pipe included in the plurality of pipes further comprises graphene deposited on the nickel.

14. The heat exchange apparatus of claim 13, wherein the graphene has a thickness of about 1.0 nm to about 10.0 nm.

15. The heat exchange apparatus of any one of claims 12-14, wherein the nickel has a coating thickness of less than about 2 micron.

16. The heat exchange apparatus of any one of claims 11-15, wherein the transfer fluid comprises a polar, non-ionizing solvent.

17. The heat exchange apparatus of claim 16, wherein the polar, non-ionizing solvent includes one or more of: acetone, ethanol, or tetrahydrofuran.

18. A method for forming a heat exchange component comprising: depositing a metal on a substrate; and coating the metal deposited on the substrate with a graphene layer using atmospheric pressure chemical vapor deposition.

19. The method of claim 18, wherein coating the metal deposited on the substrate surface comprises: heating the substrate after depositing the metal to about 900 °C to about 1100 °C; exposing the heated substrate to a gas comprising methane for a reaction time; and decreasing the substrate temperature after the reaction time at a cooling rate.

20. The method of claim 19, wherein the gas further comprises an inert gas.