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Since the first commercially successful design was introduced by APV's founder Dr Richard Seligman, the plate heat exchanger has become one of the most versatile and cost-effective methods the indirect heating and cooling of fluids. The basic concept is to run fluids on either side of a thin metal plate so that heat may be transferred between the two fluids. Product range Quotation.
APV heat exchanger plates come in over 34 different corrugation patterns and 60 different sizes, so that the heat exchanger be matched to a particular duty. The largest frame accommodate up to 1000 plates, giving a heat transfer area of more than 3500 in a single heat exchanger. The plates are typically 0.4 0.6 mm thick. Features/benefits
The PHE occupies far less floor space and weighs much less than a tubular exchanger (shell & tube heat exchanger) the same application. The smaller size means reduced capital outlay stainless steel, titanium or other costly metals. The ease of disassembly and reassembly facilitates cleaning and can make downtime purpose minimal. Up to 100 heat recovery be achieved. Low liquid hold-up avoids thermal breakdown of heat sensitive liquids. The turbulent flow reduces fouling and sedimentary deposits to an absolute minimum. Plates different but compatible geometry be alternated to regulate heat transfer to meet precise process demands. The number of plates in a frame may be increased or reduced, and plate flow patterns (i.e. thermally hard or soft) be varied to meet changed process requirements.
PRINCIPLE AND CONSTRUCTIONPRINCIPLE OF THE PLATE HEAT EXCHANGER A plate heat exchanger consists of an edge clamped frame in which a number of cold pressed plates compressed. These CONSTRUCTION OF THE PLATE HEAT EXCHANGER HeadFollower End support Flow plate Plate pack Bottom bar Tie bolts Connector grid Connector boss made special corrugations which ensures turbulent flow and high heat transfer coefficients.Example of plate heat exchanger coated stainless steel.Connector grid and connector bosses only used in plate heat exchangers two or more sections. PLATES
milk cooler cream cooler beer cooler HT cooler LT cooler central cooler sea water cooler beer chiller water chiller plate heater plate cooler genuine and original Spares and spare parts: heat exchanger spares , heat exchanger gaskets, heat exchanger rubber After clamping of the plate pack, the plates - which fitted gaskets - ensure, an effective seal between fluids and atmosphere In addition, intermixing of the fluids is eliminated by a double gasket seal around the inlet ports.
Every second plate is turned through 180 degrees. means that the double gasket seal occurs around every second inlet to the channels between the plates. The plate pack now ms a series of parallel flow channels in which the fluids flow in a counter currentregime.
Connector grids be inserted in a plate heat exchanger operating simultaneously several media. These connector grids divide the plate heat exchanger in separated s. The connector grids equipped exchangeable connector bosses.
The connector bosses form the connecting link between the respective s of the plate heat exchanger and/or connections pipes. Two connecting branches be provided in the same connection boss connection to their respective .
Plate heat exchangers more than one requiring no inlet/outlet branches in the separation be equipped separating plates (strong sheet, 2-10 mm) or flow plates equipped reinforced blankings. ASSEMBLY DRAWING Normally, an assembly drawing will be attached to the plate heat exchanger. shows all principal dimensions as well as connection specifications and identification. Show examples of the construction of a plate heat exchanger:
HEAD, Connector grid, Follower, Horizontal connection, Vertical connection, CONFIGURATION OF THE DIAGRAM.The plate pack is suspended between the head and the follower. The gasket side of the plates always face towards the head. On the right-hand side of fig. 8 be seen a single plate viewed from the gasket side. The corner holes of the plate designated
lnter-connecting lines have been drawn from the plate pack to the four corner holes of the plate. The flow channels each fluid are marked a thick or a thin line to ease identification. EXAMPLE the same plate heat exchanger a heating and cooling separated by a connector grid G1.
The cold fluid enters the heating via H1 in the head and flows through two parallel channels in one pass before entering the cooling via hole 4 in the connector grid. From here the fluid is cooled in two passes, each two parallel channels, before leaving the plate heat exchanger through F4 in the follower.
The heating medium enters through head H3 in HEAD and leaves again through head H2 in HEAD. The cooling medium enters through follower F3 in FOLL. and leaves through the connector boss of the connector grid G13H. REFERENCE NUMBER AND PUNCH CODE. The material quality and the four first digits of the reference number. of the plate stated in the top left-hand corner of the diagram.
The four last digits of the eight-digit reference number placed on the plate together a punch code. The code indicates which corner holes open to allow fluid flow. example: 1204 means that plate is open in corners whereas corner 3 marked 0 is closed.
The letter H at the top is explained in SERIAL NUMBERS. The numbers of the diagram - under the plates - serial numbers, i.e. indication of the placing of the plates in the plate heat exchanger.
Serial numbers start number 1 the head and after that continuous numbers each plate, connector grid, or separating plate. When extending the plate pack, the existing numbers used, but the new plates marked an extra figure, etc. REFERENCE NUMBERS AND GASKETS.
The diagram gives the reference number of gaskets each in the plate heat exchanger as well as quantity and reference numbers glue and cleaning fluid a complete replacement of all gaskets. CAPACITY.The data list on the diagram gives the capacities and other criteria used the design of the plate heat exchanger.
Start by erecting the head HEAD. Secure the bottom bar to the head by bolts and block it up, bolt the end support on the bottom bar. Place the follower FOLL. on two blocks approx. 200 mm from the head HEAD. Place two spacer blocks at the top between the head and the follower. Retain the follower FOLL a rope, and remove the scotching. Bolt the top bar on the end support and the head the fittings.
Fit the fittings rollers on the follower FOLL. so that the rollers exactly opposite each other. Mount the bottom bar fitting on the follower. Adjust the height of the follower by means of the roller fittings. Remove the blocks and the rope. Push the follower to the end support. Worm the plates on The top bar one by one, turn thern over the bottom bar, and push thern towards the head. Insert the plates in serial-numerical order as stated in the diagram. The serial numbers be upwards and the gasket side face towards the head.
When all the plates have been correctly assembled, push the follower against the plate pack mount the tie bolts apply a high pressure lubricant to the threaded ends of the tie bolts. Clamping should be carried out using a ratchet spanner or a similar suitable tool. Start clamping two tie bolts diagonally opposite each other. These tie bolts be tightened almost to the minimum plate pack dimension. Continue by clamping all the tie bolts in a diagonal manner.
Keep the head and the follower as parallel as possible during clamping and check at all tie bolts max. deviation 10 mm per m distance between the tie bolts). The minimum clamped plate pack dimension is shown on the machine plate on the head. MOUNTING REQUIREMENTS. The plate heat exchanger should be placed in such a way that service and inspection easily be effected. SPACE REQUIRED.
On at least one side of the plate heat exchanger there be sufficient space to unhook the plates from the top bar by a slight tilt away from the vertical. At the same time it be possible to tighten or remove the tie bolts and inspect the plate heat exchanger.
It be possible to take off the spray screen or insulating jacket, if any, out having necessarily to remove the connecting pipes. be considered when installing the unit. All engagements carried in a straight pipe out thermometer, manometer or draw off taps at a distance of 100 mm from the unit more in case of increased insulating thickness. The distance to finish insulated pipes should be 100 mm from the insulating jacket spray screen. The follower be free to move along the full length of the top bar as shown in 10. See dimensions for exactly your plate heat exchanger at the back of manual. PIPE CONNECTIONS.The plate heat exchanger be connected up according to the enclosed assembly drawing.
Threaded connections should be mounted unions or flanges plane tightening to facilitate removal - alternatively conical tightening connected to bends.
Flanged connections be removable. shows a correctly connected unit. lf necessary, a suitable filter should be installed on the fluid inlet. Insulating valves also recommended on all connections. Thermometers, pressure gauges etc. should be used as required for monitoring the plate heat exchanger performance.To prevent undue strain on the plate heat exchanger frame, all pipes be unloaded by suitable pipe holders.The pipe joints on the follower and 2 be removable in order to enable the plate heat exchanger to be opened for cleaning and inspection. For re-tightening of the plate pack, the pipes onto the follower and any connector grids be flexible. be achieved by the use of expansion joints. During opening, it be possible to move the follower, out hindrance, along the full length of the top bar. For CIP cleaning in place, out opening, piping material and layout be chosen accordingly. Piston pumps, gear pumps, dosing devices etc. not be able to transfer pressure pulsations vibrations to the plate heat exchanger as may cause fatigue fracture in the plates.
Excess pressure protector always be mounted, if the plant is likely to develop a higher pressure than that stated on the machine plate. condition may arise during pump start up, expansion or valve change over etc. The plate heat exchanger is sensitive to liquid hammering. occur during regulation, change-over, pump start-up etc., see In order to avoid situation, the use of throttling of air operated valves, damping relays in electrical control gear, automatic pump start closed valves etc. is recommended. SHIELDING The plate pack be shielded, when possible splashes may cause damage corrosive media being used the working temperature may cause scalding required by the local authorities Spray screens for all plate heat exchanger types be supplied.When thermal shielding is desirable or required, an insulating jacket be supplied.
jacket fits the heat exchanger exactly and be taken off out removing the connecting pipes. ally a drain should be located close to the plate heat exchanger. If the drain leads to public sewage system, the possible risk of pollution should be considered. If either fluid not run directly to drain, suitable spill trays should be placed beneath the unit. If necessary, these should be fitted a level alarm. START-UPPROCEDURE FOR START-UP Before the initial start-up, check that the clamped plate pack dimension is as specified on the machine plate on the plate heat exchanger Sudden surges and drops in pressure and temperature be avoided, as these may damage the plates and gaskets thereby causing leakage. Pumps should be started against closed valves which then be gradually opened until the desired flow rate is achieved.The initial start-up of plate heat exchangers new EPDM gaskets be effected by increasing the temperature slowly, max. 25C per hour.
By restart-up and stop, the following be observed Pressure surge drop not exceed 10 bar per minute. Temperature increase drop not exceed 10°C per minute. If the above precautions not observed, the guarantee will no longer apply.In a plate heat exchanger using steam as the heating media, the cold fluid should be introduced to the plate heat exchanger before the steam is turned on. The potential damage possible due to the incorrect start-up increases proportionally increased liquid flows and the length of connecting pipework For start-up of plate heat exchangers grafoseal gaskets, see During the initial start-up, minor leaks may occur until the plates and gaskets have reached their design working temperature and all s correctly pressurised. VENTING When correct working temperature and working pressure have been reached, the system be vented.The air in the plate heat exchanger is driven out by the liquid flow, provided that the capacity is as stated in the diagram. Air in a plate heat exchanger reduces the heat transmission and increases the pressure drop, thus increasing the risk of corrosion PERMISSIBLE PRESSURE Working, and testing pressures given on the machine plate.
WORKING PRESSURE the highest pressure to which the plate heat exchanger may be subjected during operation TESTING PRESSURE the pressure at which the plate heat exchanger may be tested!Pressure testing is made as a differential pressure i.e. warm and cold side separately. For plate heat exchangers several s, the stated working, testing, and differential pressures only apply if all s pressurised.If each operates at different pressures, or one of the s is not under pressure, leaks may occur in the lower pressure . The maximum permissible difference in pressure between two s separated by a connector grid or a separating plate is in general 6 kp cm. If the two s not equal in size, the permissible difference is reduced. The maximum difference in pressure depends on the number of plates in the other . pROCEDURE DURING OPERATION During operation, temperatures and pressure drops be regularly checked. Increased pressure drop and or failing temperatures indicate that there coatings on the plates. The plate heat exchanger now needs cleaning. During operation, the same precautions against rises of pressure be observed as during start-up section
TROUBLE-SHOOTING. PROCEDURE FOR STOP In plate heat exchangers for pasteurising, the steam is shut off, the hot-water pump is stopped, and the cooling fluids shut off. Finally, the product pump is stopped. If the plate heat exchanger is to be opened, it be cooled below by letting the product pump re-circulate and lowering the temperature of the circulating water by max. 10C per minute. is done by opening for the cooling water or adding cold water to the circuit. Plate heat exchangers 1 section closed down slowly so that the temperature decreases by max. 10C per minute.If there is no other possibility of cooling, the plate heat exchanger can be cooled corporation water below 40. Normally, the plate heat exchanger be unpressurised by shutting off the fluid inlets and outlets. The temperature will gradually decrease to the ambient temperature. For long working breaks, see procedure in section TROUBLE-SHOOTING In case of damage to plates or gaskets, it will often be necessary to replace them. First examine very carefully the external conditions around the plate heat exchanger in order to localise the cause of the damage!In case of fatigue fracture, will normally necessitate a replacement of all plates and gaskets as there may be a risk of fatigue fracture in all the material. In case of corrosion, all plates be examined carefully.
VISIBLE LEAKAGE When using plate heat exchangers on board ships, the follower be secured in order to avoid danger during the movements of the ship. PLATE HEAT EXCHANGERS GRAFOSEAL GASKETS When plate heat exchangers fitted grafoseal gaskets separated, these gaskets should normally be replaced by new ones. However, if the plate heat exchanger is opened, cleaned and tightened cso that the plate sequence is unchanged and no graphite material is removed fromthe plate behind, the gasket be used again. The maximum pressure will, however, be reduced somewhat. In case of replacement of a plate, the gasket in the plate behind plate be replaced as well.Grafoseal gaskets should always be handled with great care to avoid damage of the gasket surface. NOTE Never bend a grafoseal gasket CLEANING The capacities and resistance to corrosion of plate heat exchangers depend on the plate pack being kept clean. Fouling on the plates be removed manually or by CIP cleaning in place. MANUAL CLEANING Clean the plates with a soft brush and a suitable detergent. In case of thick layers of scale or organic materials, the plates be put in a bath of detergent section. NOTE.
Never use steel brush, metal scraper or the like. A high-pressure cleaner be used with care however, never with sand or other abrasives added. CIP-CLEANING A circulation system, in which a suitable detergent be circulated is established. If the product to be flushed out has a high viscosity, the circulating quantity be big enough to reach a sufficient speed flushing out the product. If the product pump is volumetric, it may be necessary to insert a pump the detergent parallel to the former. It is assumed that the fouling on the plates soluble in a detergent which does not attack plates and gaskets. Example of CIP-cleaning Drain off product residues and cooling and heating media. Rinse with cold or lukewarm water. Circulate with warm cleaning fluid solution. Rinse with warm water. Rinse with warm water with softener added to it. Rinse with cold or lukewarm water.
Cleaning also be effected without circulation by pouring a cleaning fluid solution into the system. After some time of standing, wash out the detergent with clean water.Clean plates, dirty plates, seagrass, fouled plates, cleaning agent, cleaning procedure, CONTROL OF CLEANINGThe plate heat exchanger be opened inspection at regular intervals. is necessary especially during the running in period, until experience has been gained on the effectiveness of the cleaning process. With these inspections, it will gradually be possible to determine circulation times, temperatures, and chemical concentrations with great certainty Insufficient cleaning is most often due to too small circulation quantity too short cleaning period. too small chemical consumption in relationto the fouling on the plates. too long periods of operation. If the plate heat exchanger is out of operation a long time, it is advisable to empty it, separate the plates, and clean the unit. Clamp the plate heat exchanger lightly together, and leave it covered in order to protect the gaskets against dirt and the effect of light DETERGENTSThe definition of a suitable detergent is brief and to the point. Coatings on the plates be removed without damaging plates and gaskets.
It is important not to decompose the passivating protective film of stainless steel the film contributes to preserving the resistance of the steel to corrosion. Do not use chlorine containing agents such as hydrochloric acid HCI EXAMPLES OIL AND FATS removed with a water emulsifying oil solvent, e.g. BP SYSTEM CLEANER. ORGANIC AND GREASY COATINGS removed with SODIUM HYDROXIDE NaOH max. concentration 1.5% max. temperature. 1.5% concentration corresponds to litre 30 NaOH per 100 litre water. FURRINGS AND SCALE DEPOSITS removed with NITRIC ACID HN03 max. concentration 1.5 - max. temperature 65 concentration corresponds to 1.75 litre 62% HN03 per 100 litres water. Nitric acid has an important constructive effect on the passivating film of stainless steel. CONTROL OF CLEANING FLUID CONCENTRATIONSODIUM HYDROXIDE NaOH solution is titrated with 0.1 HYDROCHLORIC ACID HCI with methyl orange or methyl red as indicator. NITRIC ACID HN03 solution is titrated with 0.1 n SODIUMHYDROXIDE NaOH with phenolphtalein as indicator. The concentration of the cleaning fluid in be calculated from the titration result according to the following formula
CONCENTRATION In order to use the correct quantity of chemicals CIP cleaning, the cleaning fluid should be checked immediately before flushing. If the concentration is too low, 0.5%, the plate heat exchanger is probably not clean. If the concentration is too high, the chemical consumption be reduced. The maximum and minimum dimension clamping is stated on the machine plate, which is placed on the head. The plate heat exchanger be clamped to dimension between max. and min. dimension. The final clamping to minimum dimension is recommended after approx. one month's operation alternatively, immediately after installing new plate heat exchangers/new gaskets. New gaskets in EPDM quality clamped step-wise the first time Minimum dimension 15% - 2 hours interval or more 3A standard dimension between max. and min. dimension as stated on the machine plate, alternatively min. dimension.The head and the follower be exactly parallel. FDA approved. ISO 9001 Certified.
Therefore, clamping be measured at the top, in the middle, and the bottom on both sides.Plate heat exchangers with Grafoseal gaskets, see section REPLACEMENT OF PLATES AND GASKETS MARKINGThe plates marked with material codes and reference plus codes non-glue gasket, if any, and also have the letter H. Looking towards the gasket side, the plate is designated a right plate when the H is upwards and a left plate when the H is downward.Left plates have inlet and outlet via corner holes 1 and 4, respectively. Serial (pleasesingle plates) In th single pass non-food PHEs Material code Four last digits of H Four last digits of the reference num- the reference of the plate ber of the plate(only on plates Right plates have inlet and outlet via corner holes 2 and 3, respectively.
right plate REPLACEMENT OF PLATES Before inserting a spplate in the plate pack, it be checked that the spare plate is identical with the defective plate - the same corner holes open, and the mark H face right.If the width of new plates is not the same as that of the plates they to replace - or of those of the plate pack being extended, the widest plates to be fitted at the back of the plate pack, if possible; adjacent to the grid, separator plate or follower. New plates always differ from old plates. Therefore, new plates to be grouped together, if possible.As an example, the current, nominal width of K-range plates is 483 mm. Previously it was smaller.A defective 4-hole plate be removed from the plate pack without inserting a spare plate, if the adjoining 4-hole plate is also removed. The new of plates will then be. changes the clamping measure of the plate pack to M1 which will be:
relation to the original of plates. At the same time, thepressure drop will increase. As to corrosion and fatigue fracture of plates, see section trouble shooting. Ordering procedure plates be found in section REPLACEMENT OF GLUED GASKETS The first plate after the head and the connector grid have a gasket in groves. These gaskets are, in fact, two gaskets cut in half and glued in place around grooves. You should carefully note how the old gaskets are assembled before removing them REMOVAL OF OLD GASKETS PLIOBOND glued gaskets be loosened by heating in water at 100C (212F).The plates cleaned, and coatings, if any, removed. See CLEANING New gaskets and the gasket grooves of the plates are cleaned with a cloth moistened with degreasing agent.
The gluing surfaces be absolutely clean without finger prints etc. As degreasing agent use what is stated on the enclosed diagram. Alternatively, use TRICHLOROETHYLENE, CHLOROTHENE VG, ACETONE, METHYL ETHYL KETONE or ETHYL ACETATE. It is important that the degreasing agent has evaporated, before the glue is applied. This will normy take approx. 15 min. at 20C (68F). It is advisable to clean the gluing surfaces of the gaskets with fine grain sandpaper instead of degreasing agent GLUING PLIOBOND 25, which is a nitrile nbr rubber glue on solvent basis 25% solids, is applied with a brush in a thin layer on the backs of the gaskets. The gaskets put to dry in a clean and dust free place The gasket grooves of the plates now coated with a thin layer of glue, and the gaskets cemented into the grooves. The insertion of gaskets starts at both ends of the plate and continues with the straight s along the edges. The gluing process is most easily effected by laying the gaskets and the plates on a table as the gaskets cemented into the grooves of the plates, the plates should be stacked. The plates with the gaskets now suspended in the frame which is clamped lightly, rubber gaskets to the minimum dimension indicated on the machine plate plus 0.2 mm per plate. The plate heat exchanger is heated to 90-100 C 94-212 F by means of water or steam.
the temperature be kept 1 - 2 hours The liquid pressure be kept as low as possible. On plate heat exchangers food, pipe branches which not connected to water steam be kept free, in order to permit glue vapours to escape!If there is no possibility of heating the plate heat exchanger, it stand at a place as warm as possible with dismounted connections. The drying time will at 20C 68F be approx. 48 hours. At e.g. 40C 104F, the drying time is reduced to approx. 24 hours service.When the glue vapours have vaporized, the plate heat exchanger be clamped again as stated in NON GLUE PARACLIP GASKETSPARACLIP is a non glue gasket designed as a conventional gasket. It is designed with a special clip on feature which locks it into recesses in the gasket groove on the plate. When replacing PARACLIP gaskets, the old gasket is removed completely. Bee fitting the new PARACLIP gasket, check that the plate gasket groove is clean and free from residual rubber, particularly in the clip-on pockets. New gaskets be fitted without using tools.The first plate after the head and the connector grids, which have no physical contact with the product, equipped with a glued gasket as described, see
However, it will seldom be necessary to change these as their only purpose is to fill out the gasket groove thereby supporting the rest of the plate pack. The PARACLIP gasket is available food as well as non-food purposes. When assembling, the EPDM quality gasket should be wiped with a cloth wetted with silicone oil to facilitate the separation from the connecting plate when disassembling the plate pack. RECONSTRUCTION rebuildingThe modular construction of the plate heat exchanger ensures an easy extension or reduction in the capacity.In case of reconstruction, the customer has to do is to state the type designation, serial number and the wanted change. APV Heat Exchanger has relevant data in file and immediately submit a suggestion and a quotation the reconstruction.SPARE PARTS AND ACCESSORIES ORDERING PROCEDURE When ordering plates, please state the serial s of the plates and the type and serial of the plate heat exchanger.
The serial s of the plates be found in the top right-hand corner of the plates the type and serial of the plate heat exchanger be taken from the machine plate In the case of single pass non-food PHEs the serial is not stamped on to the plate. ORDER EXAMPLE DDMM Pasilac Therm A/S Regards, APV Products, Kolding, Denmark Stephan Dall E-Commerce Business Development tel. dir. +4576324058 Portable phone + 4540343675 Design your Plate Heat Exchangers at 4 plates with glued on gaskets, serial s plate heat exchanger type H17 serial . ORDER EXAMPLE OF A COMPLETE SET OF PLATES:1 complete set of plates with glued-on gaskets - plate heat exchanger type M107 serial number. ORDER EXAMPLE OF A COMPLETE SET OF PLATES ONE 1 complete set of plates with glued-on gaskets the heat recovery - plate heat exchanger type K55 serial number. The plates marked with a material code symbolizing the steel quality. The four digits after the letter APV's internal press operation number three digit number and a letter. When knowing the material code, APV Heat Exchanger procure a certificate of the plate.
phone +4570278444 +4570278278 +4575503434 +4575501133 De Danske Mejeriers Maskinfabrik AmbA, Paasch & Larsen, Paasch Silkeborg, 6000 Kolding Denmark, Danmark, Olaf Ryesgade 7, Apv Baker, APV Heat Transfer, Code no, 75523511, 75523511, bestillings nr, reservedelsnumre, PVV Division, Code nos. of spares plate packings, Plattendichtung, APV Heat Exchanger A/S
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