ASHRAE OR-05-10-1-2005 Brazed Plate Heat Exchangers and Their Applications《钎焊板式换热器及其应用》.pdf
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1、OR-05-1 0-1 Brazed Plate Heat Exchangers and Their Applications Eric Mencke Jenny Larsson Ylva Persson Andreas Olsson Adam Dahlquist Patrik Eriksson ABSTRACT This paper presents an overview of brazed plate heat exchangers and their applications and competing technolo- gies. First, an illustration of
2、the construction of the brazed heat exchanger and the basic refrigerant cycle is made. Further, the paper explains where the heat exchangers can be used in a refrigerant system. Diflerent refigerant applications with brazedplate heat exchangers arepresented, liquid chillers and residential heat pump
3、s, among others. In addition, the paper compares the performance of brazed plate heat exchangers with that of shell-and-tube and coaxial heat exchangers. A brazed plate heat exchanger that solves the same operating case as a shell-and-tube is considerably smaller and lighter. The brazed plate heat e
4、xchanger is also approved for higher working pressure. At equal performance, the comparison between a coaxial evaporator and the corresponding brazed plate heat exchanger, according to tests, shows that the brazed plate heat exchanger is about ten times more weight eficient than the coaxial evaporat
5、or. INTRODUCTION The compact brazed heat exchanger (CBE) is one of the most efficient ways to transfer heat from one medium to another. A CBE consists of corrugated plates combined to create complex channels through which a hot medium and a cold medium can be alternately distributed. The mediums com
6、e into close proximity inside the CBE, on either side of the corrugated plate without mixing, and energy is transferred from one to the other as they flow side by side. The modular product concept, with customizable parts, means the right product solution for every application can often be found. Th
7、e effective use of the material in a CBE leads to a compact and very competitive heat exchanger when compared to shell-and- tube and coaxial heat exchangers. CONSTRUCTION There are several different types of CBEs depending on their material combinations and design pressures. They are defined as stan
8、dard CBEs, all-stainless CBEs, Mo-steel CBEs, and high-pressure CBEs. The basic construction materials indicate the types of fluids that can be used with the CBEs. Typical examples are synthetic or mineral oil, organic solvents, water (not seawater), glycol/water mixtures, and refrigerants (e.g., HC
9、FCs, HFCs, HCs). The standard plate materials are stainless steel, vacuum-brazed with a pure copper filler or a nickel-based filler. Carbon steel can be used to some extent, e.g., for certain types of connections. For demanding applications, the plates can be made of SMO 254, a stainless steel with
10、a higher content of molybdenum. CBEs are available in standard pressure rating or high pressure rating. In principle, the CBE is constructed as a plate package of corrugated channel plates between the front and rear cover plates, the thickness ofwhich depends on pressure ratings. The cover plate pac
11、kages consist of sealing plates, blind rings, and cover plates, as shown in Figure 1. The type of connection can be customized to meet specific market and application requirements. During the vacuum-brazing process, a brazed joint is formed at every contact point between the base and the filler mate
12、rial, which depends mainly on the working fluids. For instance, copper filler would be avoided for ammonia applications. The final design creates a heat exchanger consisting of channels with two separate circuits (Figure 1). The authors are with SWEP International AB, Landskrona, Sweden. 02005 ASHRA
13、E. 81 3 Figure 1 CBE plate package (top) and the direction of a counter-current flow through a CBE (hottom). The front plates of the CBEs are marked with an arrow. The purpose of this arrow is to indicate the front of the CBE and the location of the inner and outer circuitslchannels. With the arrow
14、pointing up, the left side (ports F 1, F3) is the inner channel and the right side (ports F2, F4) is the outer channel. The pressure drop over the outer circuit is lower because it contains one more channel. The inner circuit consequently has a slightly higher pressure drop. Ports FlIF2/F3/F4 are si
15、tuated on the front of the heat exchange and ports PllP2P31P4 are situated on the back. High turbulence is desirable for efficient heat transfer and is achieved by increasing the disturbances in a flow. A rough surface, which is achieved in the CBEs through a herringbone pattern, thus results in a m
16、ore turbulent flow than a plane surface. As the fluid passes through the channels in a CBE, it constantly changes its direction and velocity. This ensures turbulent flow even at very low flow rates and pressure drops. In addition, a turbulcnt flow will keep particles in the fluid in suspension, Le.,
17、 no particles are allowed to collect on the surface, which will avoid surface fouling. MAIN FUNCTION IN REFRIGERANT SYSTEMS Since the copper brazed plate heat exchanger became commercially available in the early 1980s, new applications have been found every year. The refrigeration industry was one b
18、usiness area that very soon realized and accepted the advantages of this hermetic, pressure resistant, compact, and highly efficient heat exchanger technology. Higher demands on efficiency and compactness for refrigeration systems have then improved the market penetration of CBEs as evaporators and
19、condensers for increasingly large capacities. The simplest refrigeration system consists of an evapora- tor, a compressor, a condenser, and an expansion valve, where CBEs typically are used as evaporators and condensers. Evaporators In all reftigerant applications, it is very important that every re
20、frigerant channel is surrounded by a secondary fluid channel on both sides. Normally, the refrigerant side is connected to the left-hand side and the secondary fluid circuit to the right-hand side on the front plate of the CBE. If the refrigerant and secondary fluid connections are transposed, the e
21、vaporation temperature will fall, with the risk of freezing and very low performance. CBEs specially optimized for evaporator duties are equipped with a special distribution device at the refrigerant inlet. The purpose of the distribution device is to distribute the refrigerant-normally made of a mi
22、xture of vapor and 81 4 ASHRAE Transactions: Symposia Figure 2 A wuter-cooled chiller; dimensions: 150 x 125 cm. liquid-evenly in the channels. The distribution device is composed of so-called v-rings, placed at the inlet of each chan- nel, forming a smooth consistent tube for the refrigerant mixtur
23、e. Each device has a carefully defined radial drilled hole, through which the refrigerant flow is forced. The posi- tion of each device at the entrance to each refrigerant channel ensures an even distribution and a stable and highly efficient heat transfer for large plate packs and high refrigerant
24、flows. Condensers When used as a condenser, the refrigerant is connected to the left connections and the secondary fluid circuit is connected to the right connections on the front plate of the CBE. As with evaporators, a countercurrent flow is the normal flow arrangement, resulting in the highest me
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