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em novembro 07, 2020

so2 scrubber design calculation

flue gas desulfurization “scrubbers”. Solving for estimated pressure drop. Considering 20% safety factor, HETP = 0.8450653m For separations, requiring 15 to 25 theoritical stages, a 15% design safety factor can be applied. control acid gas emissions, monitoring scrubber liquid pH is an adequate surrogate for scrubber liquid outlet concentration. • Maintaining 24/7/365 operation and maximizing system uptime. Amount of air taken into the lungs in a single breath. They are used . • Operating area Baltic Sea and North Sea • Finnish flag, classification society GL A full commercial project 12 / %PDF-1.4 %���� x�b```f``j``a`�cd@ AV6�8GA@Ä\� ��N-``nn�R%��W�u�H�Xt�b 120 0 obj<>stream Impingement-plate scrubber - vertical scrubber with horizontal plates, air flows from bottom to top, water flows from top to bottom ; Spray nozzle scrubbers - water are sprayed with high pressure through nozzles to produce the droplets in the air; Typical Scrubber Data. Sulfur Dioxide Scrubbing Using Caustic. 1 0 obj << /S /D >> endobj 2 0 obj << /Nums [ 0 1 0 R ] >> endobj 3 0 obj << /Type /Pages /Kids [ 8 0 R ] /Count 1 >> endobj 4 0 obj << /CreationDate (D:20040721193613Z) /ModDate (D:20100629102009-07'00') /Producer (Acrobat Distiller 5.0.5 \(Windows\)) /Author (James Eldridge) /Creator (PScript5.dll Version 5.2) /Title (Microsoft Word - SO2 Design Example.doc) >> endobj 7 0 obj << /Type /Catalog /Pages 3 0 R /Metadata 51 0 R /PageLabels 2 0 R >> endobj 8 0 obj << /Type /Page /Parent 3 0 R /Resources << /ColorSpace << /CS0 13 0 R /CS1 48 0 R /Cs6 13 0 R >> /ExtGState << /GS0 44 0 R /GS1 47 0 R >> /Font << /TT0 10 0 R /TT1 11 0 R /TT2 18 0 R /TT3 19 0 R /TT4 31 0 R >> /XObject << /Im0 43 0 R >> /ProcSet [ /PDF /Text /ImageC ] >> /Contents 49 0 R /MediaBox [ 0 0 612 792 ] /CropBox [ 0 0 612 792 ] /Rotate 0 >> endobj 10 0 obj << /Type /Font /Subtype /TrueType /FirstChar 32 /LastChar 120 /Widths [ 278 0 0 0 0 0 0 0 333 333 0 0 278 333 278 278 556 556 556 556 0 0 556 556 556 556 278 0 0 0 0 0 1015 667 0 722 0 667 0 0 0 278 0 0 556 833 722 0 667 0 722 0 611 0 0 0 0 0 0 0 0 0 0 0 0 556 0 500 556 556 278 0 556 0 0 0 222 833 556 556 556 0 333 500 278 556 0 722 500 ] /Encoding /WinAnsiEncoding /BaseFont /LCALCO+Arial /FontDescriptor 14 0 R >> endobj 11 0 obj << /Type /Font /Subtype /TrueType /FirstChar 32 /LastChar 117 /Widths [ 278 278 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 667 944 0 0 0 0 0 0 0 0 0 0 556 0 556 556 0 0 556 222 0 0 222 0 556 556 0 0 333 500 278 556 ] /Encoding /WinAnsiEncoding /BaseFont /LCALFP+Arial,Italic /FontDescriptor 12 0 R >> endobj 12 0 obj << /Type /FontDescriptor /Ascent 905 /CapHeight 0 /Descent -211 /Flags 96 /FontBBox [ -517 -325 1082 998 ] /FontName /LCALFP+Arial,Italic /ItalicAngle -15 /StemV 0 /FontFile2 42 0 R >> endobj 13 0 obj [ /ICCBased 37 0 R ] endobj 14 0 obj << /Type /FontDescriptor /Ascent 905 /CapHeight 718 /Descent -211 /Flags 32 /FontBBox [ -665 -325 2028 1006 ] /FontName /LCALCO+Arial /ItalicAngle 0 /StemV 94 /XHeight 515 /FontFile2 38 0 R >> endobj 17 0 obj << /Type /FontDescriptor /Ascent 891 /CapHeight 0 /Descent -216 /Flags 98 /FontBBox [ -547 -307 1206 1032 ] /FontName /LCALHA+TimesNewRoman,BoldItalic /ItalicAngle -15 /StemV 133 /XHeight 468 /FontFile2 41 0 R >> endobj 18 0 obj << /Type /Font /Subtype /TrueType /FirstChar 32 /LastChar 174 /Widths [ 250 0 0 500 0 833 0 0 333 333 0 570 250 333 250 0 0 500 500 0 500 500 0 500 500 500 0 0 0 570 0 0 0 667 667 667 722 667 0 0 0 0 0 0 611 0 722 722 611 722 667 556 0 722 0 889 0 0 0 0 0 0 0 0 0 500 500 444 500 444 333 500 556 278 278 500 278 778 556 500 500 500 389 389 278 556 444 667 500 444 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 500 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 747 ] /Encoding /WinAnsiEncoding /BaseFont /LCALHA+TimesNewRoman,BoldItalic /FontDescriptor 17 0 R >> endobj 19 0 obj << /Type /Font /Subtype /TrueType /FirstChar 32 /LastChar 186 /Widths [ 250 0 0 0 0 833 0 180 333 333 0 564 250 0 250 278 500 500 500 500 500 500 500 500 500 500 278 0 0 564 0 0 0 722 667 667 722 611 556 722 722 333 0 0 611 889 722 722 556 0 667 556 611 722 0 944 0 0 0 0 0 0 0 0 0 444 500 444 500 444 333 500 500 278 278 500 278 778 500 500 500 500 333 389 278 500 500 722 500 500 0 0 0 0 541 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 333 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 250 0 0 310 ] /Encoding /WinAnsiEncoding /BaseFont /LCANJF+TimesNewRoman /FontDescriptor 20 0 R >> endobj 20 0 obj << /Type /FontDescriptor /Ascent 891 /CapHeight 656 /Descent -216 /Flags 34 /FontBBox [ -568 -307 2028 1007 ] /FontName /LCANJF+TimesNewRoman /ItalicAngle 0 /StemV 94 /XHeight 0 /FontFile2 39 0 R >> endobj 31 0 obj << /Type /Font /Subtype /TrueType /FirstChar 32 /LastChar 32 /Widths [ 278 ] /Encoding /WinAnsiEncoding /BaseFont /LCBCFK+Arial,BoldItalic /FontDescriptor 32 0 R >> endobj 32 0 obj << /Type /FontDescriptor /Ascent 905 /CapHeight 0 /Descent -211 /Flags 96 /FontBBox [ -560 -376 1157 1000 ] /FontName /LCBCFK+Arial,BoldItalic /ItalicAngle -15 /StemV 133 /FontFile2 40 0 R >> endobj 37 0 obj << /N 3 /Alternate /DeviceRGB /Length 2575 /Filter /FlateDecode >> stream Usually a collection tank is nothing but a vessel which contains water / caustic lye, This particular blog entry provides a design only for non-packed spray towers for flue gas desulfurization and should not be used for any other absorber calculation. Hope this clarifies your queries. H2s Scrubber Design Calculation detailed design of each of the scrubber systems are also presented (e.g., materials of construction, solubility, heat of reaction, and operating temperature and equilibrium limits). Gas flow rate. Exhaust gas flow rate affects the L/G ratio, which is a key design parameter for wet scrubbers. "F$H:R��!z��F�Qd?r9�\A&�G���rQ��h������E��]�a�4z�Bg�����E#H �*B=��0H�I��p�p�0MxJ$�D1��D, V���ĭ����KĻ�Y�dE�"E��I2���E�B�G��t�4MzN�����r!YK� ���?%_&�#���(��0J:EAi��Q�(�()ӔWT6U@���P+���!�~��m���D�e�Դ�!��h�Ӧh/��']B/����ҏӿ�?a0n�hF!��X���8����܌k�c&5S�����6�l��Ia�2c�K�M�A�!�E�#��ƒ�d�V��(�k��e���l ����}�}�C�q�9 0000002577 00000 n Venturi Scrubber Design Equations Formulas Calculator Air Filtration, Quality, Purification and Pollution Control. • Containerships VII, scrubber delivery in August 2011 • Main stream scrubber for W ärtsilä 7L64 main engine, 12600kW • Vessel built 2002 (Sietas, Hamburg). For example, the removal efficiency of a 2 stage scrubber operating at 90% removal in each stage is calculated as: 1-(1-.90)*(1-.90) = 99% removal. 1.4 Objectives Through our research we aim to design and develop a biogas purification system which is very economical, as well as, environment friendly. Calculation ln HETP = 0.8374366 HETP = 2.3104368ft = 0.7042211m For separations, less than 15 theoritical stages, a 20% design safety factor can be applied. To read a published paper and develop an excel spreadsheet to do the calculation of this venturi scrubber design, compare the results with that of a standard venture scrubber. Inputs: venturi wet scrubber design calculation pdf slidegur com. Sulfur dioxide (SO 2) is common in flue gasses from many combustion processes. Online Library H2s Scrubber Design Calculation Controls 2 The overall removal is the product of the two individual removal efficiencies. 0000001180 00000 n (0.5 liters in an average adult) Vital capacity. Search Search PURER, G. A. DEASON I OF * Approved for public release; , J 1"73 distribution unlimited NAVAL COASTAL SYSTEMS CENTER PANAMA CITY, FLORIDA 32407.85 .U 15 (O H���yTSw�oɞ����c [���5la�QIBH�ADED���2�mtFOE�.�c��}���0��8�׎�8G�Ng�����9�w���߽��� �'����0 �֠�J��b�

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