vapor pressure of oil at different temperatures

0000006274 00000 n 0000120722 00000 n <>stream x�s x�s 0000118055 00000 n Acrobat Distiller 8.1.0 (Windows); modified using iText 4.2.0 by 1T3XT Vapor Pressure in Moist Air - Vapor pressures vs. dry and wet bulb temperature in moist air Water - Density, Specific Weight and Thermal Expansion Coefficient - Definitions, online calculator, figures and tables giving Density, Specific Weight and Thermal Expansion Coefficient of liquid water at temperatures ranging from 0 to 360 °C and 32 to 680°F - in Imperial and SI Units ͐,.�. %%EOF VoR endobj 1 0 obj 0000003586 00000 n 0000090492 00000 n <>>>/BBox[0 0 625.44 818.36]/Length 46>>stream endobj �r� 0000120466 00000 n 0000006546 00000 n endobj Data 2013.58:2898-2903Elena M. Fendu and Florin Oprea 44 0 obj 2013-11-06T12:27:56-05:002020-11-25T04:01:14-08:00Arbortext Advanced Print Publisher 10.0.1465/W Unicode <>>>/BBox[0 0 625.44 818.36]/Length 46>>stream endstream 0000011753 00000 n endstream K'2X����e ���Ze���;�#��~W~��NV���z}������{��s�52� ���u����E�l����,��%?�ՀfIz�/����=^? �% endobj trailer �% 0000015496 00000 n ͐,.�. 29 0 obj �r� <>>>/BBox[0 0 625.44 818.36]/Length 47>>stream 0000057371 00000 n endstream 0000058700 00000 n 0000015245 00000 n x�+� � | 0000004336 00000 n �% x�S�*�*T0T0 B�����ih�����]�"� �S _ x�+� � | Online calculator. endstream 0 0000091918 00000 n endstream 23 0 obj 0000092771 00000 n 15 0 obj ��w3T�PI�2T0 BCcC#=s#C#��\. 0000017258 00000 n ��w3T�PI�2T0 BCcC#=s#C#��\. 0000117759 00000 n �% Recalculation of density of oil for different temperature and pressure values. 0000000016 00000 n 0000006411 00000 n endobj ͐,.�. 43 0 obj endobj 0000014040 00000 n x�s <>>>/BBox[0 0 625.44 818.36]/Length 47>>stream endobj Vapor Pressure, also known as bubble point pressure and accurate vapor pressure, is the pressure where the primary bubble of vapor is shaped at a given temperature. As a result, sealed containers of volatile liquids are potential bombs if subjected to large increases in temperature. endstream x�S�*�*T0T0 B�����ih�����]�"� �� W "State system for ensuring the uniformity of measurements. Chem. Issue10.1021/je4004977 Data 2013.58:2898-2903je4004977 1..6J. endstream 0000014950 00000 n x�S�*�*T0T0 B�����i�����U�"� �n Ln�p����lF0� �K��`2lZ*�d|rĞ�D2���$50[H�g�2�Ul/# ���%? endobj 0000001696 00000 n ?����#�j�"%�?��_o������q���I>���qs������� �Ӻ�~j��~��t�FA���J�J�/�7W��SО��'��2���^���4Ȫ����}iN&���p�q)� ˯o�۵�mv�j�Uk���2�X���Y�a���V�}s�ᵏt�u�7���Q6j}�]��ƾ����^�..?�2^�������,���%�|5v�7e���r5$��u��H瓖�����aeS endstream x�s 0000014235 00000 n ��w3T�PI�2T0 BCcC#=s#c��\. 0000058948 00000 n application/pdfJ. 0000090211 00000 n endobj 5 0 obj <>stream 28 0 obj 'cC ��w3T�PI�2T0 BCcC#=s#c��\. endstream 0000002723 00000 n 18 0 obj ͐,.�. <>stream endstream x�b```e``gb`c`���A��b�,?��c`���� ��I�*�a��f����MM��b:. In turn, changes in temperature have an impact on vapor pressure. �M5˧�I�T�� monitor vapour pressure at different temperatures and V/L ratios will allow the operator to regulate their transportation system immediately. <>>>/BBox[0 0 625.44 818.36]/Length 47>>stream Density of oil. 0000002135 00000 n endstream ?B����.��6̌�d/����Kw)�x��a�ay�Das�"9o���Y��V�^��Խ�����d����Ed�*��x���鈥 װ@��e�kY��N:�=:��كZ/��dj���q�Qv�&�"q˻�4�$���y�����߷,�+5z +;�_���҉_��Z��fTt��0צ&�Y�&��L^a����dD���n���۷�����~y� 3s8g� �bW�f���#��ܘ���]m��ė�q"�������7{� #��9w�z-�WF{O��;�"�lͶ1���"�ز�]�oK7���y�Y$�cx������ؖ���:r_&��e��_]��N�껴S{�r�Q�D�D�堍�4mA (��Rt:S��^ۃ��I�'��A h��-�Τ�AȠ�A§�O /^��g�$�)8S�D h�b```���B�� ��ea�hphQ )20���j��P��z�x���ٌ̛u�:�)p�� *�6Rct`�wP)Pt�Y�{��깻w��:(��|V�� ���'{�e&O�.�6Y��4PB��pG�,?��YaE�M:��\l.O����t���g�b�'��nv�f�3��%r�GK��g�%��b��yrz� ��s>�sSJ�sg���L���ӦΙ� ���������� S)�� ��4:؀� �J e@9���� "� �� ����b� 1s���� A majority of the vapor pressure testers can measure crude oil at a V/L ratio of 4/1 and only at 37.8 °C. x�s endobj <>>>/BBox[0 0 625.44 818.36]/Length 46>>stream 0000013771 00000 n 0000092839 00000 n endobj 0000013904 00000 n 0000090279 00000 n �r� <>stream 0000121093 00000 n ͐,.�. Exponential temperature variation fit. endobj 3 0 obj x�s 0000117827 00000 n 100 0 obj<>stream endstream x�S�*�*T0T0 B�����ih�����]�"� �� [ <>stream ��w3T�PI�2T0 BCcC#=s#C#��\. 0000089890 00000 n endobj endobj 0000010747 00000 n 7 0 obj Vapour pressure. 0000014596 00000 n <>>>/BBox[0 0 625.44 818.36]/Length 47>>stream x�ͻ�0D��_1e"��c���UR-]� Db ��������m�D�;�&�� �\u�����F,��; AZ <>>>/BBox[0 0 625.44 818.36]/Length 46>>stream <> 17 0 obj 12 0 obj endobj ��w3T�PI�2T0 BCcC#=s#C#��\. d4����7031�p9pOhue�dxPq��)��ef�S�3�c�aЉ2e��p(v�3��8� �?�]���d�8h�P��z����>3�2*����1�G�x%@� epoY Click here for an illustration. 19 0 obj 0000090143 00000 n 31 70 ͐,.�. �r� endstream ��w3T�PI�2T0 BCcC#=s#c��\. �% x�+� � | endobj �% Composition. hެ{�r$Ǒ���>�}��eͪ5D1��7^e�,E�3�9ՅbwIX� ���~����9�I�lES#�23.~9��Ӆ[�m5��uh����"���~�e?��*a(�C���Y�\|�٩.6��[�6B��;�x{��I�A�s�q�A�Zl����ŰX���/�}��+2�4��uy9Hc1����PV1���O���_��ć�4���������sU��T�s��7Ϙ��ws�m�/���mo��-�k���" q�j\ >-�[��ai��[k|�i�I���/ܰ�j�� �+]�4���Y��l.1X�����36?���R:�i��� �Ͼ��g>�-�����M�q��r���xa���Z��*��^��^>}}��`�kaV^5���jm�^X�Ve���5ea S��� �y���?׷�����,�9nO����#�Ж�ooN��GRqU���;m�/y���bcՖ��\o�J��k|y�Q2. 24 0 obj ͐,.�. 0000023230 00000 n 11 0 obj endstream endobj startxref endobj 0000007131 00000 n ͐,.�. 1448 0 obj <>stream <>stream endstream endstream 0000092415 00000 n endstream Vapours are heavier than air (2 to 3 times). 0000120790 00000 n x�s 0000118451 00000 n 0000017598 00000 n %PDF-1.3 endobj 0000014926 00000 n endobj 31 0 obj <> endobj ͐,.�. &� 0000115956 00000 n %PDF-1.4 %���� �, ڦ-nwP�lӒe]�9'�tI�*�����P^ֿ����cÅG�Ue�0�;Y�ZD��OSpk�4���Ҁ�`�*��v4�E��@��4I��)�4?�@���$/1�0d3�1p1��|������PȐ�G�5�%����%c�5��̻r 0000005067 00000 n <>stream endstream 0000002233 00000 n %PDF-1.6 %���� 0000005179 00000 n endobj <]>> Vapour pressures of diesel at room temperature are very low; that discussed in has a vapor pressure of 0.4 mm Hg (E 0.053 kPa). 26 0 obj 0000121069 00000 n 0000092169 00000 n 0000091527 00000 n xref �B3:H*��%���b)p�'20�3{21�`�Ƹ�����0S�gf����3�&e8)t@L�. endobj 10 0 obj measured as a function of temperature: vapor pressure (409.85 to 582.15) K, density (298.15 to 443.15) K, viscosity (288.15 to 393.15) K, and surface tension (298.15 to 468.15) K. The obtained data for tetrapropylene glycol were regressed using correlations from simulation software.

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