Proyecto fin de carrera: Sustitución de central térmica en una fábrica de refinado de aceite y envasado. Paraffinic Hydrocarbon (Single Cut)

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A.4. CARACTERISTICAS DEL ACEITE TERMICO Paratherm HE High Flash & Fire Points, Thermally Stable HEAT TRANSFER FLUID TYPICAL PROPERTIES* Physical Properties Feedstock Paraffinic Hydrocarbon (Single Cut) Appearance Odor Optimum Use Range Flash Point (coc) ASTM D-92 Fire Point (coc) ASTM D-92 Autoignition ASTM D-2155 Transparent, Pale Yellow Faint (oily) 15 F to 6 F (66 C to 316 C) 44 F (227 C) 5 F (26 C) 7 F (371 C) Atmospheric Boiling Point, 1% Fraction, ASTM D-116 779 F (415 C) Vapor Pressure, psia @ 3 F.39 35 F.193 4 F.97 45 F.387 5 F.135 55 F.387 6 F.87 Coefficient of Thermal Expansion**.592/ F.166/ C Heat Of Vaporization (Calculated) 77.19 BTU/lb Heat Of Combustion 19,55 BTU/lb API Gravity ASTM D-287 31.7 Specific Gravity @ 15 C ASTM D-1298.8651 Density, lb/gal @ 6 F (16 C) 7.22 Viscosity: cst @ 4 C ASTM D-445 4.25 Pour Point (Crystal Point) ASTM D-97 5 F (-15 C) Pumpability: Centrifugal @ 2, centipoise, nominal 2 F (-7 C) Color ASTM D-15 1. Molecular Weight ASTM D-252 445g/mole Corrosivity (3hr Cu Strip @ 1 C) ASTM D-13 1A

Total Sulfur (Mass%) J-14.2 Total Acid Number (T.A.N.) ASTM D-664.1 Electrical Properties Dielectric Strength @ 2 C, nominal >3 KV/cm Optical Properties Refractive Index ASTM D-1747 1.4722 *These are typical laboratory values, and are not guaranteed for all samples. **Note: Normal practice is to size the expansion tank so that it is 1/4 to 1/3 full when the system is cold, and 2/3 to 3/4 full when the system is at the maximum normal operating temperature. Tabla de datos (SI Unidades) Rev. 1 Temperatura Densidad Viscosidad C F g/ml kg/m3 cst (m¾/s) cp (mpa-s) Calor específico Conductividad térmica 32.8755 876 453 396.4328.1347 5 41.8724 872 33 264.4371.1343 1 5.8692 869 21 182.4415.134 15 59.866 866 152 131.4458.1336 2 68.8628 863 112 97.452.1332 25 77.8596 86 84 72.4545.1328 Presión de vapor cal/(g- C) W/(m-K) mm Hg kpa 3 86.8564 856 65 55.4588.1325.1 35 95.8533 853 51 43.4632.1321.1 4 14.851 85 4.3 34.2.4675.1317.1 45 113.8469 847 32.5 27.5.4719.1313.1 5 122.8437 844 26.6 22.4.4762.131.1 55 131.845 841 22.1 18.5.486.136.1 6 14.8342 837 18.5 15.5.4849.132.1 65 149.8342 834 15.8 13.1.4892.1299.1 7 158.831 831 13.5 11.2.4936.1295.1 75 167.8278 828 11.7 9.71.4979.1291.1 8 176.8246 825 1.2 8.44.523.1287.2 85 185.8214 821 9.1 7.4.566.1284.2 9 194.8182 818 7.98 6.52.511.128.2 95 23.8151 815 7.11 5.79.5153.1276.2 1 212.8119 812 6.37 5.17.5196.1272.2 15 221.887 89 5.74 4.64.524.1269.2 11 23.855 86 5.2 4.19.5283.1265.2 115 239.823 82 4.74 3.8.5327.1261.2 12 248.7991 799 4.34 3.46.537.1257.2 125 257.796 796 3.99 3.17.5414.1254.2 13 266.7928 793 3.68 2.91.5457.125.3 135 275.7899 79 3.4 2.68.55.1246.3 14 284.7864 786 3.16 2.48.5544.1242.3

145 293.7832 783 2.94 2.3.5587.1239.3 15 32.78 78 2.75 2.14.5631.1235.3 155 311.7769 777 2.57 1.99.5674.1231.5.1 16 32.7737 774 2.41 1.86.5718.1227.7.1 165 328.775 77 2.27 1.75.5761.1224.8.1 17 337.7673 767 2.15 1.64.584.122.1.1 175 346.7641 764 2.3 1.55.5848.1216.12.2 18 355.769 761 1.92 1.46.5891.1212.19.3 185 364.7577 758 1.83 1.38.5935.129.26.3 19 373.7546 755 1.74 1.31.5978.125.32.4 195 382.7514 751 1.67 1.25.622.121.39.5 2 382.7482 748 1.59 1.19.665.1197.46.6 25 4.745 745 1.52 1.13.618.1194.68.9 21 49.7418 742 1.47 1.9.6152.119.94.13 215 418.7386 739 1.42 1.5.6195.1186 1.2.16 22 427.7355 735 1.37 1.1.6239.1182 1.46.19 225 436.7323 732 1.33.971.6282.1179 1.72.23 23 445.7291 729 1.28.931.6326.1175 2.36.31 235 454.7259 726 1.23.892.6369.1171 3.9.41 24 463.7227 723 1.18.854.6412.1167 3.83.51 245 472.7195 72 1.13.815.6456.1164 4.56.61 25 481.7164 716 1.9.777.6599.116 5.3.71 255 49.7132 713 1.4.739.6543.1156 6.79.9 26 499.71 71.99.72.6586.1152 8.47 1.1 265 58.768 77.96.678.6629.1149 1.2 1.4 27 517.736 74.935.657.6673.1145 11.8 1.6 275 526.74 7.91.637.6716.1141 13.5 1.8 28 535.6973 697.88.612.676.1137 16.5 2.2 285 544.6941 694.855.592.683.1134 19.8 2.6 29 553.699 691.83.572.6847.113 23.2 3.1 295 562.6877 688.85.552.689.1126 26.5 3.5 3 571.6845 685.78.533.6933.1122 29.8 4. 35 58.6813 681.755.513.6977.1119 34.6 4.6 31 589.6782 678.73.494.72.1115 39.3 5.2 315 598.675 675.77.476.764.1111 44.1 5.9 32 67.6717 672.69.463.746.117 49. 6.5 325 616.6685 668.674.45.729.113 54. 7.2 33 625.6652 665.657.437.711.199 59. 7.9 335 634.6619 662.641.424.6994.195 64. 8.5 338 64.6587 659.625.411.6977.191 69. 9.2

Paratherm HE HEAT TRANSFER FLUID High Flash & Fire Points, Thermally Stable ENGINEERING BULLETIN HE 32 Precise, Uniform Temperature Control TM in Closed-Loop Heat Transfer Systems The Paratherm HE high flash and fire point heat transfer fluid is rated for an optimal service range of 15 F to 6 F (66 C to 316 C). Engineered for higher thermal and oxidative stability, it is efficient and cost effective. Its greater purity allows it to strongly resist degradation while holding thermal properties and maintaining efficiency. This provides for low maintenance and solid performance over an extended operating life. Non-toxic, the HE fluid is safe to use and easy to dispose. It can be safely combined with spent lubricating oils and recycled locally. Found in a broad variety of applications, the fluid is recommended, specified and/or approved by a host of equipment manufacturers and thermal fluid heater OEMs for continuously operated systems. Recognized by U.L. (Underwriters Laboratories, Inc., No. MH17163-N), the durable HE fluid has a proven record of success under demanding conditions and yet is safe and easy to handle. Safety in Operation The Paratherm HE fluid has among the highest flash and fire points of any high temperature heat transfer fluid. With a flash point of 44 F, and a fire point of 5 F, it is an extremely safe fluid to have in your system. In many cases, these flash and fire points exceed the system s operating temperature. The HE fluid is Coast Guard approved for molten sulfur service and has passed rigorous Bioassay with 3 species. Human/Environmental Safety The Paratherm HE fluid is virtually non-toxic. With an Oral LD 5 rating of >35 (the higher the number, the lower the toxicity), the HE fluid is actually safer than most oils. In the event of a release, it can be treated using the same simple clean-up procedures used for light lubricating oils. Once gathered and placed in a container, the HE fluid can be combined with the plant s used lubricating oils and sent to the local recycler. Have the Material Safety Data Sheet available for the recycler. Note that the HE fluid contains no chlorinated hydrocarbons, and virtually no polar compounds, sulphur, oxides of nitrogen or heavy metals. Corrosion in the System The HE fluid is manufactured from natural feedstocks, and provides similar metal-coating Typical Properties* Physical Properties Feedstock Paraffinic Hydrocarbon (Single Cut) Appearance Transparent, Pale Yellow Odor Faint (oily) Optimum Use Range 15 to 6 F (66 C to 316 C) Flash Point (coc) ASTM-D-92 44 F (227 C) Fire Point (coc) ASTM-D-92 5 F (26 C) Autoignition ASTM-D-2155 7 F (371 C) Atmospheric Boiling Point, 1% Fraction, ASTM-D-116 779 F (415 C) Vapor Pressure, psia @ 3 F.39 35 F.193 4 F.97 45 F.387 5 F.135 55 F.387 6 F.87 Coefficient of Thermal Expansion**.592/ F.166/ C Heat of Vaporization (Calculated) 77.19 Btu/lb Heat of Combustion 19,55 Btu/lb API Gravity ASTM D-287 31.7 Specific Gravity @ 15 C ASTM-D-1298.8651 Density, lb/gal @ 6 F (16 C) 7.22 Viscosity, cst @ 4 C ASTM-D-445 4.25 Pour Point (Crystal Point) ASTM-D-97 5 F (-15 C) HE-L/P TM Fluid -35 F Pumpability: Centrifugal @ 2, centipoise, nominal 2 F (-7 C) Color ASTM-D-15 1. Molecular Weight ASTM-D-252 445g/mole Corrosivity (3hr Cu Strip @ 1 C) ASTM-D-13 1A Total Sulphur (Mass %) J-14.2 Total Acid Number (T.A.N.) ASTM-D-974.1 Electrical Properties Dielectric Strength @2 C, nominal and lubricating properties as the finest natural oils. However, any water allowed to stand in piping, components or especially expansion tanks of thermal oil systems can cause corrosion. Because the Paratherm HE fluid is immiscible with water and also slightly less dense, any water can be easily drained from the system s low point drains. Crack the low-point valve and allow fluid to drain into a beaker or clear water glass. If your see a phase separation (one liquid floating on top of the other), continue to drain until no separation is observed. >3 KV/cm Optical Properties Refractive Index ASTM-D-1747 1.4722 * These are typical laboratory values, and are not guaranteed for all samples. ** Note: Normal practice is to size expansion tanks so that they are 1/4 to 1/3 full when the system is cold, and 2/3 to 3/4 full when the system is at the maximum normal operating temperature. Storing Your Fluid Drums of heat transfer fluid should be kept in non-hazardous dry areas. Until ready for use, the container s tamper evident safety seals must remain intact. Liquids should not be allowed to pool on the tops of the drums. In the afternoon and evening when temperatures cool, the heat transfer fluid will cool and contract slightly. A partial vacuum is created in the drum, and, if the bung s elastomeric seal is not perfect, liquid standing on the top of the drum can be drawn through, contaminating the fluid. If drums must be temporarily stored outside, store them on their sides.

1 5 1 VISCOSITY 15 2 25 3 C 1.7 5 SPECIFIC HEAT 1 15 2 25 3 C.7 1 1.65.65 cst 1 1 mm 2 /s BTU/(lb- F).6.55.6.55 cal/ (g- C) 1 1.5.5.45.45.1.1 1 2 3 4 5 6 F 1 2 3 4 5 6 F DENSITY THERMAL CONDUCTIVITY lb/gal 7.4 7.2 7. 6.8 6.6 6.4 6.2 6. 5.8 5 1 15 2 25 3 C.85.8.75.7 g/ml BTU/(hr-ft 2 - F/ft).78.76.74.72.7.68.66 5 1 15 2 25 3 C.135.13.125.12.115 W/(m-K) 5.6.64.11.65 1 2 3 4 5 6 F 1 2 3 4 5 6 F Pre-Cleaning the System For optimal performance of both system and its heat transfer fluid, we strongly suggest that piping, valves and other components be thoroughly cleaned before installation. Mill scale, weld spatter and slag, quench oils, protective lacquer and varnish coatings, and dust and dirt can act to degrade the fluid, and can damage pumps and valves. And lodging in restrictions, these contaminants can easily create the same low flow conditions that cause premature failure of systems and fluid. Inerting the System Immediately after completing installation of the system, we suggest you purge with inert gas. Such purging can eliminate air and water vapor, and can substantially reduce corrosion. And while purging, you can leak test the system using simple soap-bubble detection. Finally, when you charge the system, any gas that becomes dissolved in the fluid will be inert, and fluid oxidation at start-up will be almost nil. Charging the System When charging the system, we suggest you fill from the bottom (a point near pump suction) using a small positive displacement pump not the system pump. Charging from the system s low point can help reduce trapped air in the system, which will substantially reduce the entrainment of gas bubbles and resultant pump cavitation. Fluid Disposal Because Paratherm heat transfer fluids are produced from natural feedstocks, they are exceptionally safe to use. Easy to dispose, used or contaminated Paratherm fluids can be safely combined with spent lubricating oils and recycled locally (EPA, citation 57FR21524). Paratherm strongly encourages recycling of used heat transfer fluid to conserve natural resources and to minimize the problem of liquid waste in landfills. We suggest you check local, state and federal regulations first, of course. (Note: liquids contaminated with chlorinated solvents or other regulated materials may require special handling, and may not be accepted by recyclers.) Fluid Analysis Overheating, oxidation and contamination of your heat transfer fluid can significantly reduce its ability to perform. Product quality will suffer, and in severe cases considerable damage to your thermal oil system can result. Periodic analysis of your fluid can allow you to detect problems in the early stages and achieve substantial savings. Quality Control We thoroughly test each batch of heat transfer fluid to ensure absolute conformance to tight production specifications. Each shipment is traceable to the master batch, with test results archived at Paratherm. 4 Portland Road West Conshohocken PA 19428 USA Phone: 61-941-49 Fax: 61-941-9191 8-222-3611 E-mail: info@paratherm.com Web: www.paratherm.com Note: The information and recommendations in this literature are made in good faith and are believed to be correct as of the below date. You, the user or specifier, should independently determine the suitability and fitness of Paratherm heat transfer fluids for use in your specific application. We warrant that the fluids conform to the specifications in Paratherm literature. Because our assistance is furnished without charge, and because we have no control over the fluid s end use or the conditions under which it will be used, we make no other warranties expressed or implied, including the warranties of merchantability or fitness for a particular use or purpose (recommendations in this bulletin are not intended nor should be construed as approval to infringe on any existing patent). The user s exclusive remedy, and Paratherm s sole liability is limited to refund of the purchase price or replacement of any product proven to be otherwise than as warranted. Paratherm Corporation will not be liable for incidental or consequential damages of any kind. 22 Paratherm Corporation Printed on recycled paper HE 32