Document VQG7NO7bL7Q6xxMNJVoX0ez8

v., -- l) ^ /'c 7 /:y Monsanto Chemicals-Plastics _ _ _ KA__ AN INDIRECT AROCLOR HEATER for UNIT CHEMICAL OPERATIONS Monsanto Technical Bulletin No. 0-130 October, 1955 Monsanto Chemical Company, Organic Chemicals Division, St. Louis 1, Mo. AN INDIRECFTORARg ONCULOR)( Mu onsanto Technical Bullotin No. 0-130 CHEMICAL OPERATIONS I Orfobe,, toss /fv'f -/?- /''s77- ;? Aroclor* 1248 (chlorinated biphenyl) is an ideal 4wiiflaimnabft liquid phase heattransfer medium for temperatures up to 600 F. This bulletin contains a magazine reprint which describes the physical properties of Aroclor 1248 and illustrates the design and operation of heaters that have been used successfully by Monsanto plants for many years. The units described are gas fired and the capacities are in the range of 200,000 to 400,000 B.t.u. per hour. Larger commercial installations using Aroclor 1248 have capacities ranging up to 2,000,000 B.t.u. per hour. Also small electrically heated stationary and portable units with capacities around 40,000 B.t.u. per hour are in service. Although the magazine reprint contained first appeared in 1949, the basic information is still valid. Since that time Monsanto has developed a considerable amount of en gineering data on heat transfer applications of Aroclor 1248. Those interested in such information are invited to correspond with the Organic Chemicals Division of Mon santo. Monsanto does not manufacture heat-transfer equipment using Aroclor fluids. It supplies only the Aroclor 1248 needed. Several leading manufacturers of heating equipment are in a position to build or offer Aroclor heating units to meet specific requirements. 0408474 *R#f. CT.S. Pat. Off. The information contained In thia bullatln la, to Our boat knowledge, true and accurate, but all recoinmendatlone or uggaatlona are made without guarantee, alnca the condition! of uae are beyond our control. The Moneanlo Chemical Company dltcialma any liability incurred In connection with the uae of theie data or luggaattona. Furthermore, nothing contained herein ehetl be conatrued aa a recommendation to uae any product in conflict with ealaltng polenta covering any matarlal or tie uaa. TOWOLDMONOQ31521 Reprinted from INDUSTRIAL AND ENGINEERING CHEMISTRY, Vol. 41, Page 1841, July 1949 Copyright 1949 bv the American Chemical Society and reprinted by permission of the copyright owner An Indirect Aroclor Heater for Unit Chemical Operations MEADE McARDLE1, L. C. GARRETT, AND P. G. BENIGNUS* Monsanto Chemical Company, Anniston, Ala. 1 he characteristics of Aroclor 1248 indicate that it Sprat Flammabiutt. When a tube ruptures in a liquid heat- is an ideal liquid phase heat-excliange medium for transfer system under high pressure, a spray or mist forms. temperatures up to 300 C. This article discusses its The possible fire hazard under these conditions requires considera properties and illustrates the design and operation of tions not covered by the foregoing discussions relative to the ma heaters that have been used successfully by Monsanto terial in the liquid form. In their comprehensive study of plants during the past seven years. flammability of the higher boiling liquids and their mists, Sulli van, Wolfe, and Zisman (0) determined the spray flammability IN CERTAIN manufacturing processes of the Monsanto limit of numerous materials in accordance with the percentage of Chemical Company, it was necessary to employ a noncom oxygen required for combustion. This value was then correlated bustible heat-traiBfer medium at pressures of 30 pounds per with the results of incendiary firing tests of the fluids conducted square inch or less and temperatures up to 3000 C. The following at the Naval Proving Ground, Dahlgren, Va. The oxygen re general properties of a heat-exchange medium were required: quirement for Aroclor 1248 combustion in the spray flammability Freedom from fire hazards. Viscosities to permit pumping at room temperatures, boiling point sufficiently above 300 C. to assure a liquid con dition at all times. Stability against heat, with enough safety factor to accommo date accidental overheating. Controllable vaporization losses. Freedom from corrosive action against valves, piping, tank jackets, etc., made of cast iron and steels, bronze, and stainless steel. Freedom from toxicity hazard. Aroclor, chlorinated biphenyl (registered in U. S. Patent limit studies was found to be 04%. Fluids requiring over 45 to 50% oxygen in the spray test failed to cause a fire in the incendi ary test. These results establish the nonflammable and noncom bustible qualities of Aroclor 1248. VISCOSITY CONSIDERATIONS Cold Flow. For most inside installations centrifugal pumps will handle Aroclor at reduced rates without preheating. Experi ence confirms this. Outside installations have been started at 0 C. by heating the pump and feed fine until circulation through Office), was selected. The pertinent physical characteristics relative to its use ns a heat-transfer medium are given in Table I. Table I. Physical Properties op Aroclor 1248 FRFFDOM FROM FIRE HAZARDS Flash Point. Limitations of this test for the prediction of the fire hazard of relatively nonvolatile organic fluids have been recognized by the American Society for Testing Materials com mittee (5, J,). Fire Point i6 a more significant measurement. The Under writers' Laboratories (10) state that fire tests more truly reflect the (lack of) fire hazard of Aroclor. Spontaneous Ignition Temperature. The combustion- resisting qualities of Aroclor 1248 are indicated by its high spon taneous ignition temperature of 704 C. (1299 F.) determined by Sullivan, Wolfe, and Zisman (9), using the convenient apparatus described by Sortman, Beatty, and Heron (8). Under conditions of industrial use the spontaneous ignition temperature will be determined by factors including the nature of the hot surface, the amount oT liquid impinging on it, the volume of enclosed space, and the ventilation. An accidental failure in a heating system demonstrated the nonflammability of Aroclor 1248 and ita freedom from the hazard of fire propagation. An operator'6 failure to start the circulation of the heat^transfer medium when the gas heater was on resulted in excessive coil temperatures and caused the lower coil to soften and sag into the fire chamber. A weld ruptured and Aroclor 1248 poured into the red-hot fire chamber in contact with the flame. Dense smoke arose from the heater but there waB no external fire. After the gas flame was cut off, the smoking stopped. * Present address, Monsanto Chemical Company, Organic Chemicals Division, Bl. Louie. Mo. 1 Present address, Monsanto Chemical Company. Phosphate Division, St. Louis, Mo. Appearance Absolute density, g./ml. Practically colorless mobile liquid C. ( F.) 1.44 1.41 1.37 1.27 1.17 30 (80) 60 (140) 100 (212) 200 (392) 300 (672) Absolute viscosity, centipoises Thermal conductivity. B.t.u./hour/sq. foot/ 0 F./foot Distillation range. A.S.T.M. D*20, C. Flash point, Cleveland open cup, A.S.T.M. D 92-45, 6 C. Fire point, Cleveland open cup, A.S.T.M. D 02-45 Pour point, A.S.T.M. D-7, * C. Coefficient of expansion, ml./ml./ C. (25-- 65 C.) Specific volume, ml./g. 112 17.6 4.2 0.69 0.47 0.0613 0.0098 0.0800 340-375 193-190 0 000702 0.696 0.709 0.728 0.787 0.660 30 (86) 60 (140) 100 (212) 200 (392) 300 (672) 30 (86) 60 (140) 100 (212) 30 (86) 60 (140) 100 (212) 200 (392) 800 (572) Specific heat, oal./g./ C. 0.383 0.307 0.326 0.355 M> 1133) 100 (913) 300 093) 300 (572) Vapor pressure, mm. Hg 0.00037 0.16 2.0 18.0 160.0 87.8 100 160 200 300 ((2110201 (802 (572) 0408475 TOWOLDMONOQ31522 1342 INDUSTRIAL AND ENGINEERING CHEMISTRY Voi. 41, No. 7 Table II. Stability of Aroclor 1248 Heated for 30 Hours Temperature, Mg. of HCl per Gram of Aroclor 280 0.070 810 0.109 320 0.222 30 0.248 Table III. Stability of Aroclor 1248 Continuously Heated at 280 and 330 C. Hour* Mg. of HCl per Gram of Aroclor 280 C 330 C. 30 0.070 0.248 60 0.116 0.610 00 0.160 0.023 120 0.104 1.141 150 0.261 1.862 Table IV. Gas Analysis of Aroclor 1248 Heated 4 Hours at 260 C. and 210 Pounds per Square Inch Pressure Rt 340 C. fitted with an internal gas burner bo that the gas flame impinged directly on the surface of the Aroclor. Analysis of the gases produced under these conditions included 0.6% carbon monoxide, 0.17% oxygen (derived from the air), 0.99% hydrogen chloride, 2.1% combustible gas calculated at methane, 0.002% chlorine, and no phosgene. The same workers studied the stability of Aroclor when heated for 4 hours in an iron pipe at 260 C. under an internal pressure of 210 pounds per square inch, resulting from the introduction of compressed air. Following this treatment and cooling, the easel removed from the system were analyzed. The acidity of the Aroclor was determined prior to and after exposure to these con ditions. The results given in Table IV reflect an extremely small amount of decomposition under conditions similar to those selected for the practical use of Aroclor 1248 as a heat-transfer medium. In actual practice using the type of heating unit described below there has been no evidence of hydrochloric acid effect and no car bon deposits have been noted in the heater, pipes, or valves. The heaters have been operated successfully with combustion gases at approximately 600 C. in contact with the coils. Chlorine Acidity (% by weight HCl) Prior to exposure After exposure 0.2 None None 0.0076 0.0075 the heater had been effected so that the system could operate Dormally. BOILING POINT Operating experience has shown that the boiling point of Aro clor 1248 (340 C. at 760 mm.) is enough above the 300 C. operating limit to prevent trouble from this cause. At the maxi mum operating temperature the vapor pressure is less than 0.5 atmosphere. HEAT STABILITY In order to establish a maximum practical operating tempera ture, the stability of the material when heated to elevated tem peratures in the presence of iron was noted. A slow stream of nitrogen was passed over the hot Aroclor to sweep the decom position products into a caustic trap. The amount of acidic material was determined and calculated as hydrochloric acid. The results given in Table II indicate the stability of Aroclor 1248 when individual samples were heated for 30 hours at the given `mperatures. The decom position is very low at temperatures up to 300 C. The stability of Aroclor J 248 in contact witli L iron continuously heated at 280 and 330 C. is indicated by Table III. These test results indi cate that Aroclor 1248 in con tact with iron can be used satisfactorily at temperatures up to 300 C. The National Board of Fire Underwriters (/0)reported that "decomposition of the product (Aroclor 1248 j was not appreci able at temperatures below 400 C., but became increas ingly apparent at higher tem peratures." Their workers analyzed the decomposition products of Aroclor 1248 heated in the pres ence of hot iron at 469 C. and also heated iu an iron cylinder END ELEVATION At one time, a spiral coil typo of heater was built and through faulty design a burner tunnel was located 1.6 inches from the 2inch steel pipe coil. The radiation from the white-hot refractory tunnel ana the direct impingement of the flarne on the pipe caused the pipe to glow a dark red for a space of about 2 inches. This unit was operated almost 3 months before a circulation stoppage occurred. When the line was opened lumps of carbon were found to have come loose and moved forward to lodge in the globe valves. The lumps measured about. 1 X 2.5 cm. and one face was formed to fit the pipe curvature. No hydrochloric acid effect was noted and the system was put back into operation after the burner location was changed. CONTROLLABLE VAPORIZATION LOSSES The heating systems in which Aroclor 1248 is used are sealed except for the expansion tank, which has a loose cover or a vent pipe, Because this tank is separated from the stream by a sub stantia) length of pipe, the temperature in the tank remains low. In the light of the relatively low vapor pressure values for Aroclor 1248 (7), and as it is unlikely that the expansion tank will ever reach even the 1-mm. state (130 C.), there should not be measurable loss of Aroclor from the system. Actual experience bears out this contention. Other Losses. Although Aroclor darkens on use, its charac teristics remain the same and replacement has not been found necessary after 7 years of continuous use. Accidental leaks or spills constitute the only observed losses. PLAN AND PART SECTION B-B 0*08476 TOWOLDMONOQ31523 uly 1949 INDUSTRIAL AND ENGINEERING CHEMISTRY 1343 Table V. Resistance of Structural Materials to Aroclor 1248 Met*lg Aluminum Copper Mkgneiiutu Nickel Silver Tin 25 C. R 125 C. R Metals Mild steel Phosphor bronte Red Drees Stainless steel Yellow braes Re RR. Excellent reeietancc, less than 1.0 X 10~*cm. per day penetration or 0.00014 inoh per year. R. Good resistance, penetration between 1.0 X 10"* and 10 X 10** cm. per day or between 0.00014 and 0.0014 inoh per year. D. Doubtful resistance, penetration between 10 X 10"* cm. per day and 100 X 10"* chi. per day or between 0.0014 and 0.014 inch per year. e. Following letter indicating resistance, signifies material may be littr than indicated if totally immersed, as weight loss is believed to come from oxidation of part of test strip exposed to air. DESIGN AND CONSTRUCTION Heating System. The heating system required to utilize Aroclor 1248 as the exchange medium includes a heater (Figure 1), cooler, pump, and expansion tank (Figure 2), and control and safety circuits (Figure 3). FREEDOM FROM CORROSIVE ACTION The resistance of various metals (7) at 25 and 125 C. is given in Table V. Similar studies made at 325 C. (6) indicate that the penetra Figure 3. Control and Safety Circuit tion, in inches per year, for mild steel is 0.0028; for yellow brass, 0.00047; for copper, 0.00145. Many years of practical operating experience with Aroclor 1248 Heater Design. The general requirements of the heater are as a heat-transfer medium have shown that the materia) is prac compactness, ease of construction and service, and avoidance of tically noncorrosivo to valves, piping, tank jackets, etc., made direct flame impingement on the tubes. of cast iron and Bteels, bronze, and stainless steel. Direct flame impingement is prevented by directing the gas FREEDOM FROM TOXICITY HAZARD flame through an enclosed channel with half-thickness fire brick protecting the tubes above until the high temperature of the Aroclor 1248 is a very stable, unreactive liquid. If the material is spilled on the skin, there are no noticeable ill effects; however, it is well to wash the skin with soap and water after contact. name is reduced by heat conducted through these bricks and radiated to the two bottom coils. The size of the heater is reduced ttthhoeeahhmooittntteeimssttuaamrieabsy aunsdi'n2g 'ionnclhyes4.o5.fin~Ecahgelse oNfoin. s6u6laintisnuglafitri.oenborinckthine A skin burn resulting from accidental contact with hot Aroclor ciooler spots. should be treated in the normal procedure used for hot oil burns. Aroclor adhering to the burned area need not be removed im mediately unless treatment of the burn demands it; in this case Two sizes of units are used: One has a maximum capacity of 200,000 B.t.u. per hour, as shown in Figure 1. The larger has a range of 200,000 to 400,000 B.t.u. The small size consists of 90 feet of 1-inch standard weight steel soap and water or repeated washings with a vegetable oil (linseed pipe made into three coils of six pipes each and connected in oil) should be used. The vapors emitted by Aroclor 1248 heated to elevated tem peratures are injurious to the liver on prolonged exposure and series. The larger size consists of 144 feet of 1.5-inch standard weight steel pipe arranged in the same fashion. Results of testa on the small-size heater covering temperatures from 150 to 300 C. show temperature rises to 10 to 20 C. in the Aroclor should not be breathed. Drinker (5) indicated that 0.5 mg. of while circulating at a rate of 15 to 20 gallons per minute. The Aroclor 1248 per cubic meter of air is the maximum safe amount permissible in workrooms. In commercial heat-transfer installations, the presumption is outlet gas temperature is consistently within 75 C. of the outlet Aroclor temperature. It is observed that the bottom two coils ab sorb the major part of the heat. The small unit indicates 50 to 60% efficiencies for capacities up to 200,000 B.t.u. per hour when & that the Aroclor is in a closed system free from leaks. Accord natural gas of 1000 li.t.u. per cubic foot is burned. A Surface ingly, there should lie no opportunity for workers to come in codtact with vapors from the hot heat-transfer medium. Combustion Company high pressure inspirator and tunnel burner set is used in this installation. Over-all heat-exchange coefficients (Cr) for the furnace are in the range of 7 to 10 B.t.u. per hour per square foot per degree Fahrenheit. Over-all heat-exchange coefficients for Aroclor 1248 <SHFtt' to water in a double pipe heal-exchanger made from 1.25-inch pipe with a 2-inch pipe jacket are in the 120 to 180 range. These figures are calculated from test results on this STEAM Oft installation. WATER YOUTLET Cooler. A very useful adjunct to the system is a double pipe cooler on JACKETED PIPE COOLER -Qh the outlet of the heater shown in Figure 2. By turning water into the jacket, the Aroclor can be cooled and DRAIN --tXj-HX- the temperature of the system lowered. This is helpful when it is necessary to coo) a batch before removing it or POMP I when an exothermic reaction starts to O-txj. get out of control. Pump. The pump for circulating the Aroclor 1248 may be any one of a HEATER PIPING number of standard centrifugal units Figure 2. Coaler, Pump, and Expansion Tank designed for hot liquid service. 0 *0 8 *7 7 TOWOLDMONOQ31524 1344 INDUSTRIAL AND ENGINEERING CHEMISTRY Vol. 41, No. 7 Pipe Construction die, (ccs, and reducers Flanges Bolts Unions Dope Gaskets Shut-off valves Control valves Cheek valves Belief valves Valve stem parking (inge am! glass Strainers Table VI. Pihng Detail (Dimensions in inobes) */ through */, 'A through /, 1 throug' 6 V through Y 1 through C V*through V V. through i/ 1 through 2 2V, through ft V* through */ 1 through 2 V. through y, 1 through 2 1 /, through 3 '/< gage */-*/ 1 through 3 Schedule 80, A.S.T.M. A53 or AI06 Schedule 40, A.S.T.M. A53 or A106 Sorewed Flanged Ruud in shop and field where pos sible. Must be cleaned to remove scale Forged steel screwed. Crane 3O0d series Welded fittings. Crane 300o Series 30 (to match valves) Machine bolts A.S.A. B-18.2 with hex agonal nuts for service below 500 F. Above use alloy steel. Crane tri plex A.S.T.M. ABO Crane 252h forged stee (Irani* 425 high tem perature thread compound Soft iron ring fiat or corrugated Crane 3G0GW, screwed, gate Cram* 3G15W, flange, gute Crane 33XR, flange, gate Crane 3G40 XH, screwed, globe Crane 3G5G XR, flange, globe Crane 151 XR, flange, globe Crane 3674 X, screwed Crain* 3G8G X, flanged Crane 159 X, flanged Consolidated H>70 B , screwed Consolidated 1012 W , flanged (ioelre 340 D or Duratnetallie I>110 Type 100 PCPR Marsh 0-100 inch gage siphon with Crane 222H bar stock valve, .lerguson Series R20 Reflex type li'piid level gage 82! Ynrwny threaded 822 Varwav flanged The Dayton Dowd Type (' pump is an example of the type required. It- should l>e made of east steel and have a watercooled stuffing box and water-cooled bearings. The stuffing box Bhould have room for at least six rings of packing and a lantern ring. Duramelallic No. D-110 or Oarlock No. 234 may be used for packing the pump. An open impeller is desirable, as it will handle the cool, more viscous liquid on starting the system better than will a closed imjH'llcr. Lnough horsepower for the most viscous conditions is required. I'ihno System and Expansion Tank. The detail of the piping system for Aroclor 1248 used up to temperatures of 300 C. (572 F.) and 100 pounds per square inch pressure is giveu in Table VI. The valves and specialties giveu indicate the type re quired. AH piping larger than 0.75 inch is flanged or welded; ex perience has shown that hot. Aroclor penetrates screwed joints of the larger sizes. Steel and cast steel are used throughout. The system requires an expansion tank located at the highest level of the installation. The size of this tank is normally about 25% of the capacity of the Aroclor system. Connections with valves, made on either side of the pump, enable the operator to connect, a flexible hose and to pump in or out as required. For operation in locations where the Aroclor temperature may drop to where the attendant viscosities may make pumping im practical in the system as designed, it may be desirable to steamjacket the Aroclor circulating lines to facilitate rapid start-up. Suitable safety provisions, such as safety pop-off valves, must be installed in the steam jacket system to prevent pressure ruptures which would develop if any condensate remained in a closed sys tem during high temperature operation. In order to establish operating conditions and to check the operation of the heater itself, it is often desirable to measure the temperatures of the Aroclor in and out of the heater and cooler. Items 9,10, and 11 (Figure 2) provide for this. They may be dial thermometers or mercury bulb thermometers of any commercially available type recommended for the service. VII.Table Safety and Control Equipment 1. High pressure alarm Mercoid DA-31, open circuit on high pressure. (detects stoppage Actual settings depend on individual layout of pipe) 2. Low pressure alarm Mercoid DA-31-3, open circuit on low pressure. (detects stoppage Actual settings depend on individual layout of pump) 3. Thermostat (detects Fenwal 18002. Contacts open on temperature excessive heating increase hence obstruction of flow) 4. Float switch (detects Mercoid Figure 40. S.P. switch. Open at low leakage from sys level tem) 5. Flame failure system Combustion Control Corp. Fireye FF6. Flame (cuts off gas if failure control for manual ignition gas burner pilot flame goes systems out) 6. Gas valve (cuts off General Control Corp. K-10-2. Closes with in case preceding current off devices act) 7. Red light (alarm) Killsrk VA-1 60 W, or Beniamin 7013-V 8. Horn (sounds alarm) Edwards 312 Alarm relay Type C-1104 1-NO, 1-NC watertight (1) Stop horn relay Type C-1104 1-NO, 1-NC, watertight (/) Stop horn button l-llA-4 () 9. Thermometer well 0 360 C. mercury bulb thermometer (visual check of heater perform- 10. Thermometer well 0 300' C. mercury bulb thermometer (visual check of heater perform ance) 11. Thermometer well 0-360 C. mercury bulb thermometer (visual check of cooler perform ance) 12. Solenoid valve General Control K-10-2. Controls Aroclor temperature to meet demands of system For automatic temperature control a solenoid valve, item 12, is indicated in a by-pass arrangementwith a manually operated needle valve. The needle valve is adjusted to give almost enough heat to meet the requirements and the actual control is carried on by the solenoid valve, which opens and closes ns directed by a tem perature-control instrument connected to the equipment being heated. One unit was set up with temperature control using a Leeds & Northrop Model S all-electric control with droop corrector. Very close control over a wide range of heat demand resulted, when a throttling range adjustment of 4 was used on this control device. Safety Circuit. Figure 3 shows a safety circuit which auto matically protects the system by closing off the gas supply in the event of faulty operating conditions. Provision is made for shutting off the warning horn while the system is being put back into operation after a safety shutdowu. A detailed list of the safety and control equipment is given in Table VII. The equipment named indicates the type required. ACKNOWLEDGMENTS The authors are grateful to A. M. Ellenburg of Monsanto's Re search Laboratory at Anniston, Ala., for furnishing many of the technical data about Aroclor 1248 and for assistance in preparing the manuscript. LITERATURE CITED (1) Allen Bradloy Co., Milwaukee, Wis., Bull. 700. (2) Ibid., Bull. 800. (3) Am. Soc. Testing Materials, Proc. Am. Soc. Testing Materials, 34,53 (1934). . (4) Am. Soc. Testing Materials, "Standards on Petroleum Prod ucts and Lubricants," 1945. (5) Drinker. C. K., J. Ind. Hyg. Toxicol., 21, 155 (1939). (6) Monsanto Chemical Co., Anniston, Ala., private communica tion, April 13, 1944. (7) Monsanto Chemical Co., St. Louis, Mo., Monsanto Tech. Bull. P-115 (August 1947). (8) Sortman, C., Bcattv, H., and Heron, S., Ind. Eng. Cbeu., 33, 357(1941). (9) Sullivan. M. V., Wol/e. J. K., and Zisman, W. A., Ibid., 39, 1007 (1947). (10) Underwriters' Laboratories, Chicago, 111., "Miscellaneous Hazards," No. 2498,1934. Received August 27, 1948. Presented before the Meeting-in-Miniature, Alabama Section, American Chemical Societt, December 8. 1945. Pointed in U. S, A. 0406473 TOWOLDMONOQ31525 HEATER FOR U N IT CHEMICAL OPERATIONS / Monsanto Chemicals-Plastics KA Monsanto Technical Bulletin No. 0 -1 3 0 October, 1955 For further information on the product! described in this bulletin contact the nearest Monsanto office. MONSANTO CHEMICAL COMPANY ST. LOUIS AKRON ATLANTA BOSTON CHICAGO CINCINNATI CLEVELAND DETROIT HOUSTON LOS ANGELES MINNEAPOLIS NEW YORK SAN FRANCISCO SEATTLE WILMINGTON MONSANTO CHEMICALS LTD. London MONSANTO CHEMICALS (AUSTRALIA) LTD. Melbourne MONSANTO (CANADA) LTD. Montreal Toronto Vancouver Representatives in the Principal Cities of the World 0408479 TOWOLDMONOQ31526