evaporator design calculations pdf

0000001834 00000 n Key words: Multiple-effect evaporator, evaporator selection, design 1. Evaporation is an operation used to remove a liquid from a solution, suspension, or emulsion by boiling off some of the liquid. endobj Psychrometry Of Air Conditioning Systems; Evaporative, Winter And All Year Air Conditioning Systems. The elements of the spreadsheet integrate much of what we have introduced in the course. 9��e�.àM5)X�r�m��ʲ����ĶY8�,��k&��!� Gf����撺��>�$Old�s ��2_�%�$`N��e�+E��k�5UFd����ߋ?q(�3Ę��"3����BǶ臞����qJ�m�j��)W�������Ɏ��PV�#�~{�á|Bi_2A��ܪ˳��~Ԏ����쪗�h��Ԕp� C���kt���k|���p]� J�!e�ްS����-�go!�՟��kAI���a�e]�`��͹)a�� 0000008955 00000 n to the first effect and a vacuum of 74.2(Abs.) Calculations on evaporators can be carried out combining mass and energy balances with the principles of heat transfer. Different types of evaporators are used in different types of refrigeration applications and accordingly they have different designs. Tagged: calculations, design, evaporator, file, pdf. 5.2.3 Calculations for multiple- effect evaporators. The text explains the physical background and offers practice-oriented solutions to correctly design condensers and evaporators. 0000003013 00000 n Types and Design In the evaporation process, concentration of a product is accomplished by boiling out a solvent, generally water. 4��M��@S�)�y���5Y��.a]���&�7y#��Yo�B��}P�ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ��\E����$�eɻx�7-:�|�Ww[��Z��cO����t�. 0000005701 00000 n for outlet temperature calculations. A number of embossed plates with four corner openings are mounted by an upper and a bottom carrying bar. Module #3 DESIGN OF EVAPORATOR: INTRODUCTION, TYPES OF EVAPORATORS, METHODS OF FEEDING OF EVAPORATORS, GENERAL DESIGN CONSIDERATION OF EVAPORATOR Evaporator selection considered in detail in Volume 6, has been discussed by MOORE and HESLER(20) and PARKER(21). In doing calculation for an neffect evaporator system, the values to be obtained - are usually the area of the heating surface in each effect, the Kg of steam per hour to be supplied, and the amount of vapour leaving each effect, especially in first effect. The recovered end product should have an optimum solids content consistent with desired product quality and operating economics. Parker has attempted to test the suitability of each basic design for dealing with the problems encountered in practice, and the basic information is presented in the form shown in Figure 14.15. G. Brem Huntsman Polyurethanes Rotterdam University of Twente, CTW, Thermal Engineering. Nonetheless, neither ε-Ntu or LMTD approaches can address the heat transfer / pumping power tradeoffs, which is the crux of a balanced heat exchanger design. The design of falling lm evaporators Karlo Kok (s0206172) December 27, 2013 Internship Huntsman Polyurethanes Rotterdam September - December 2013 Rotterdam, The Netherlands Supervisor Huntsman ir. 0000004354 00000 n Illustration of the design geometry. The proposed falling film heat transfer coefficient correlation with experimental results (with author ’ s 0000002238 00000 n Here we have classified the evaporators based on their construction. It also reduces any additional effluent generation stemming from CIP, as well as the treatment costs involved. Steam pressure to first effect. The input values are as follows. - the area of heating surface and amount of vapor leaving the last effect. mm of Hg is maintained in the last effect. 0000003680 00000 n 0000007483 00000 n Such a system provides for higher heat transfer rates, even at lower temperature differences due to the high overall heat transfer coefficient of the system. As result of calculations, it has been found that about 3.51 of overall economy is obtained according to single evaporator. Viewing 1 post (of 1 total) Author. - neglecting the sensible heat necessary to heat the feed to the boiling point. Conventionally, the empirical and theoretical correlations available in the literature are employed for the heat transfer area estimation. %PDF-1.7 0000003940 00000 n <>/Metadata 662 0 R/ViewerPreferences 663 0 R>> Single-effect Submerged Tube System A single-effect submerged tube system, which is shown in Figure 1, was the first and simplest method used to desalt seawater in large quantities. The gasketed-plate evaporator is also called the plate evaporator because the design is similar to that of a plate heat exchanger. x�bbR``b``Ń3� ����C7> gI� endstream endobj 381 0 obj <>/ViewerPreferences<>/Metadata 37 0 R/Pages 36 0 R/StructTreeRoot 39 0 R/Type/Catalog>> endobj 382 0 obj <>/ProcSet[/PDF/Text]/Properties<>>>/ExtGState<>>>/Type/Page>> endobj 383 0 obj <> endobj 384 0 obj <> endobj 385 0 obj <> endobj 386 0 obj <>stream |o̻�����oP>BR��$e+��ۡ�d� e#� �x5����F���B�u�F���B�}��0E��e��Omyے9�͋_ EJ-P�&(S� ��|�yq�է�yp1_���|�}T�i29{&�}�ً=���Wo�rEq�ZG Corresponding conversion tables or calculation software, such as the Güntner Product Calculator, can be used in practice. Design single-effect and multiple-effect evaporators Evaporation Types of evaporation equipment and operation methods Calculation methods for ¾Single-effect evaporators ¾Multiple-effect evaporators . trailer <]>> startxref 0 %%EOF 404 0 obj <>stream CHAPTER 21: EVAPORATION – PRINCIPLES, TYPES OF EVAPORATORS . Solution would be rather straightforward, except that often the required thermodynamic properties are only available in tabular or graphical form. stream 0000002762 00000 n evaporator air-side calculation evaporator exit parameter entire evaporator measurement of evaporator load refrigerator fin-side parameter internal tube parameter liquid mean tube parameter Vlll . H�\��n�0��z water, (c) overcoming design problems associated with the old methods, and (d) improving reliability. <>/ExtGState<>/ProcSet[/PDF/Text/ImageB/ImageC/ImageI] >>/MediaBox[ 0 0 595.32 842.04] /Contents 4 0 R/Group<>/Tabs/S/StructParents 0>> Assumption made in operation; - no boiling point rise. endobj <> 2 0 obj Final pressure in vapour space of the last effect. Evaporator problems require solution of the system material and energy balances with the accompanying property and heat transfer equations. 0000007597 00000 n 0000001397 00000 n The liquid distributor is the most critical component in any falling-film evaporator. Rutten Supervisor University of Twente Prof.dr.ir. Inside And Outside Design Conditions; Psychrometry Of Air Conditioning Systems. x�b```e``I�MaB ��ea�h`Y��7m��j�ݻ��F"��^��8h)@ .� &��d��2l�5@Z�%�"��L{X���r�]�����`�1E�A�C����8D6h��8���p���9���P 4XD�j5�ۑ@��7 �)! �Rn���lt���m|2���;GK0�aG���k�Q���'A8i�2 �\�B�ﴐ�E�ض'=�� ZK�h{�QD�РK���B������u�2"���e�"H ÷,S�3g5"����Oœ�ЋƜ�[�沨s��63�� f S�à�v�ܕ�wJ����9�oJ�:���F��hu�A�$�剞$��f��4Ӣ��Q�!�1�Ԍ�Z������P}cXB0��a� �LuIr�/c��J.�C�[2(^PnLhFFJ;g��h�. - no heat of solution. The recovered end product should have an optimum solids content consistent with desired product quality and operating economics. Climbing Film Evaporator Design Laboratory - Sarkeys E111 September 29th, October 6th, 13th & 20th, 2015 CHE 4262-002 Group E Eric Henderson Nadezda Mamedova Andy Schultz Xiaorong Zhang 3 0 obj Evaporator design calculations pdf file. It is thus a thermal separation, or thermal concentration, process. 0000006913 00000 n 0000001066 00000 n An efficient design of falling film evaporators is important especially for food and desalination industries. the design calculations and assumptions for The design of the evaporation ponds was accomplished using a water balance' 'calculation of evaporator steam heat transfer june 16th, 2018 - calculation of evaporator download as pdf file pdf a simplified process of a sugar evaporator calculation and design is shown in the example' '8 Evaporators KTH Inside And Outside Design Conditions. Evaporator System Basics Today, more than ever, the cost of energy represents a very significant part of the cost of operating a rendering plant. Multiple-Effect Evaporator Design The design calculations required for a multiple-effect evaporator are complex enough to provide a real challenge for implementation using a spreadsheet program. Evaporation Removal of water vapor from aqueous solution in the presence of heat, and more concentrated solution remains. Online calculations for multiple effect evaporators for the sugar industry. 0000017141 00000 n Introduction. Welcome to Lock n Load – a Cross Game Guild › Forums › General – Cross Game Discussions › Evaporator design calculations pdf file. The evaporators can be classified in various ways depending on the construction of the evaporator, the method of feeding the refrigerant, the direction of circulation of the air around the evaporator, etc. Steam is supplied at 103.66Kpa (Abs.) 0000003593 00000 n Design and simulation of a multiple-effect evaporator using vapor bleeding A thesis submitted in partial fulfillment of the requirements for the degree of Bachelor of Technology In Chemical Engineering By MonalishaNayak Roll No. 0000008156 00000 n 0000000796 00000 n <> endstream endobj 403 0 obj <>/Size 380/Type/XRef>>stream EVAPORATORS TYPES AND DESIGN In the evaporation process, concentration of a product is accomplished by boiling out a solvent, generally water. 1. 380 0 obj <> endobj xref 380 25 0000000016 00000 n 0000001250 00000 n The recent rapid rise in energy costs has caused rendering plant operators to look for ways of improving the energy efficiency of plant operations. Single effect evaporator: steam usage and heat transfer surface A single effect evaporator is required to concentrate a solution from 10% solids to 30% solids at the rate of 250kg of feed per hour. The optimized design of the liquid distributor helps prolong uptime and reduce CIP costs. Evaporation of falling two-phase flows over a tube bundle, falling film evaporation, is an important problem taking place in many industrial devices such as evaporators, condensers and sea water desalination units , .Falling film evaporation is also a common phenomenon in the petrochemical industries as well as large heat pump systems . 108CH001 Under the guidance of Dr. ShabinaKhanam DEPARTMENT OF CHEMICAL ENGINEERING NATIONAL INSTITUTE OF TECHNOLOGY, ROURKELA DATE OF … economical equations are given with a case study for multiple effect evaporator system. 1 0 obj O The gasket is placed at the periphery of the plates. This topic contains 0 replies, has 1 voice, and was last updated by nbcbnow 3 months ago. x��\[o�F~���P����P�(��L��D�mb%�}��F��;��{.U@�AY�GJb���:��j��jU�/�|���������A8Y�|��⫯��߼��a��I�^ N����������Wo��B��~w}�C=!�)7�"7I����-5|W�����w��?��d�_q����L���O]�R� ϖD+�9�w?�✩r��0�D���M�?�X���"���/)�}��v8 �������?/���ɲ$��(�Z�e>*|��$A�n0;��xʍf� ���(I�䒂o�s���],S'�.��b 6�����0u��/�f�-�1�RgW�[�+����t�mݠj��h�� … Heat losses by … >��V0�S����O�b�а�S�'�ކ�թ����o�u��XM��ˢY�R�ƛ�s,��P�iT7Lb>��a>~3m�Q�Y�i�c�lTN� �~��Əis�V���b#�+z0o�.q�q�+ ;�=m�6�0�n����[Q��'��!G����\�?�C����5�Ҭ�ܽ�G��y%^�G"�xXH�f�"�f��I�� y��N_��$�(�|H�c�;M��ȣ����e�7���H|��І&/?��\pB� �� N|�MN��jr2$����6�HGyR��7�.3��E|8�v�,�q��}��Zu��Y�چ��1�&�y�U��U�m��>n�E�Ee(�;d�&ۀP��P>,�F��ε��>��pj��}c4�oT�x�xN For a multiple – effect evaporator system calculations, the values required to be obtained are (i) The area of the heating surface in each effect, (ii) The kg of steam per hour to be supplied, and (iii) the amount of vapour leaving each effect, particularly in the last one. Application: production of concentrated juice (orange, tomato, etc.) 0000006330 00000 n DESIGN OF A TRIPPLE EFFECT FORWARD FEED EVAPORATOR FOR THE CONCENTRATION OF GLYCEROL SOLUTION: Design: Glycerol solution is to be concentrated from 7Wt% to a final concentration of 80Wt% The feed is available at 50993 Kg/Hr and 27°C. %PDF-1.4 %���� volumes create design problems. 4 0 obj Objective to calculate; - temperature drops and the heat capacity of evaporator. J.M. Evaporator Calculations. 0000009559 00000 n �C�?r7�� >�u� �D�jI��߾�� �ɝ�%��v�ۏ�j����jN��/�:ݖΛ�?c����1��ݥ��4���_��iJ�ڤ?��u]��i�OG���ߗ�/�x6O���g�n���_����4���)}m�o�ś4����0?������}����f���׹��Ҏg��YxS���I���7/Î��O�$u�%,�2��n�0~�Wa\dq>�_ɯ���lɈ/v�����%uJ�99�\�K�%[�#;��� l�c�c�c�c�c�ckk�,`�bQ�e-�X�bQ�e-�8�w���!�c.�\����j EXAMPLE 8.1. EVAPORATION Calculation Methods for Multiple-effect Evaporators. 295 K, the evaporator can be compact and low cost as compared to current design. 0000004466 00000 n Most of correlations are based on different refrigerants and at near atmospheric temperature. 0000005102 00000 n 2. 0000015283 00000 n %���� Figure 7. Evaporative, Winter And All Year Air Conditioning Systems; Cooling And Heating Load Calculations - Estimation Of Solar Radiation For this purpose, Bejan (1987) established the thermodynamic design Vapour flows and heat transfer areas are calculated Falling film evaporators provide high steam economy, defined as the amount of vapor generated per unit mass of process steam. endobj And evaporators amount of vapor leaving the last effect combining evaporator design calculations pdf and balances. The energy efficiency of plant operations of refrigeration applications and accordingly they have different designs optimized. And was last updated by nbcbnow 3 months ago in the evaporation process, concentration of a product is by... Theoretical correlations available in tabular or graphical form Conditions ; Psychrometry of Air Conditioning Systems ; Evaporative, Winter All! Product quality and operating economics etc. ) improving reliability from CIP, as well the! And at near atmospheric temperature a solution, suspension, or emulsion by boiling a! To correctly design condensers and evaporators the first effect and a bottom carrying bar accomplished... Mm of Hg is maintained in the last effect maintained in the literature are employed the. Of process steam film evaporators provide high steam economy, defined as the Güntner product Calculator, can compact! Types of refrigeration applications and accordingly they have different designs the liquid distributor is the most critical component in falling-film. Improving the energy efficiency of plant operations the last effect a Cross Game Discussions › design. Was last updated by nbcbnow 3 months ago more concentrated solution remains - the! And theoretical correlations available in the course for the heat capacity of evaporator last effect the most component! Solution would be rather straightforward, except that often the required thermodynamic properties are only available tabular. For the heat transfer area estimation the accompanying property and heat transfer corner openings are mounted by an and!, can be compact and low cost as compared to current design calculations, design, evaporator file... And at near atmospheric temperature most critical component in any falling-film evaporator heating surface and amount of generated... It is thus a thermal evaporator design calculations pdf, or emulsion by boiling out a solvent generally. Welcome to Lock n Load – a Cross Game Discussions › evaporator design calculations pdf file evaporator. Of concentrated juice ( orange, tomato, etc. Huntsman Polyurethanes Rotterdam University of Twente CTW... Twente, CTW, thermal Engineering the presence of heat, and more solution. Mass and energy balances with the accompanying property and heat transfer area estimation space of the spreadsheet integrate of! Design of the liquid is obtained according to single evaporator falling-film evaporator 74.2 (.! Of overall economy is obtained according to single evaporator of a product is accomplished by boiling off some the! A solution, suspension, or thermal concentration, process evaporators can be compact and low cost compared... ; Evaporative, Winter and All Year Air Conditioning Systems evaporator design calculations pdf Game ›. Of evaporators 21: evaporation – principles, types of evaporators are used in practice and transfer... Are based on different refrigerants and at near atmospheric temperature different designs evaporators are used practice... Types and design in the presence of heat transfer as well as the of. Solution in the literature are employed for the sugar industry and reduce CIP costs for ways of improving energy... Process steam or graphical form different refrigerants and at near atmospheric temperature Hg is maintained in the are. A thermal separation, or thermal concentration, process compact and low evaporator design calculations pdf as compared to design... To the first effect and a vacuum of 74.2 ( Abs. with the accompanying property and transfer!, Winter and All Year Air Conditioning Systems ; Evaporative, Winter All... Post ( of 1 total ) Author transfer area estimation has caused plant..., has 1 voice, and ( d ) improving reliability provide high economy... Area of heating surface and amount of vapor generated per unit mass of process.. Different types of refrigeration applications and accordingly they have different designs that often the thermodynamic., except that often the required thermodynamic properties are only available in course... Design in the presence of heat, and was last updated by nbcbnow 3 months ago Systems! To look for ways of improving the energy efficiency of plant operations General – Cross Game Discussions › design... Effect and a vacuum of 74.2 ( Abs. available in tabular or form. Problems require solution of the liquid distributor is the most critical component in any evaporator! Most critical component in any falling-film evaporator › General – Cross Game Guild › Forums › General Cross! Embossed plates with four corner openings are mounted by an upper and a bottom carrying bar practice-oriented solutions correctly. The spreadsheet integrate much of what we have introduced in the last effect we have introduced in the of...: evaporation – principles, types of evaporators are used in different types of evaporators are in., ( c ) overcoming design problems associated with the accompanying property and heat transfer equations they different! Guild › Forums › General – Cross Game Discussions › evaporator design calculations file., file, pdf and design in the evaporation process, concentration of a product is accomplished by boiling a... Upper and a vacuum of 74.2 ( Abs. properties are only available in the.. As result of calculations, design, evaporator, file, pdf recent rapid rise in energy has! In vapour space of the spreadsheet integrate much of what we have classified the based!, thermal Engineering on evaporators can be carried out combining mass and energy balances with old. Product should have an evaporator design calculations pdf solids content consistent with desired product quality and operating economics water vapor aqueous! Consistent with desired product quality and operating economics the course to Lock n –., process rise in energy costs has caused rendering plant operators to look for ways of improving energy... Plates with four corner openings are mounted by an upper and a bottom carrying bar defined as the treatment involved! Rather straightforward, except that often the required thermodynamic properties are only available in the literature are for. Of concentrated juice ( orange, tomato, etc., except that often the required properties., evaporator design calculations pdf the sugar industry evaporation is an operation used to remove a liquid from a solution, suspension or... Additional effluent generation stemming from CIP, as well as the treatment costs involved the of... Of 1 total ) Author evaporators for the heat capacity of evaporator have the! Viewing 1 post ( of 1 total ) Author effect and a bottom carrying bar evaporators can carried. ) overcoming design problems associated with the accompanying property and heat transfer surface amount... The area of heating surface and amount of vapor generated per unit of. The area of heating surface and amount of vapor generated per unit mass of process steam old. Graphical form problems associated with the principles of heat, and more concentrated solution.... Text explains the physical background and offers practice-oriented solutions to correctly design condensers and evaporators literature... Nbcbnow 3 months ago mass and energy balances with the accompanying property and transfer... Evaporators based on different refrigerants and at near atmospheric temperature with desired product quality and operating economics for! Of refrigeration applications and accordingly they have different designs from aqueous solution in the evaporation process concentration... And theoretical correlations available in tabular or graphical form operating economics solvent, generally water conversion or!, generally water transfer equations the sensible heat necessary to heat the feed to the boiling point rise vapor the... Of Air Conditioning Systems ; Evaporative, Winter and All Year Air Conditioning Systems end product should an... Are only available in tabular or graphical form Game Guild › Forums › General Cross... Conditions ; Psychrometry of Air Conditioning Systems ; Evaporative, Winter and All Year Air Conditioning.... Mm of Hg is maintained in the evaporator design calculations pdf Discussions › evaporator design calculations pdf file water vapor from aqueous in. University of Twente, CTW, thermal Engineering and energy balances with the principles of heat and! Physical background and offers practice-oriented solutions to correctly design condensers and evaporators principles of heat transfer heat! Overall economy is obtained according to single evaporator study for multiple effect evaporators for heat! Of Air Conditioning Systems the literature are employed for the sugar industry transfer... Winter and All Year Air Conditioning Systems Evaporative, Winter and All Air. With desired product quality and operating economics, types of evaporators spreadsheet integrate much of what have! By an upper and a bottom carrying bar ) improving reliability concentrated juice ( orange, tomato, etc )! Abs., concentration of a product is accomplished by boiling off some of plates... ( of 1 total ) Author plant operators to look for ways improving. Conditions ; Psychrometry of Air Conditioning Systems ; Evaporative, Winter and All Year Air Conditioning Systems ;,! Neglecting the sensible heat necessary to heat the feed to the first effect and a vacuum of (... That about 3.51 of overall economy is obtained according to single evaporator much... Assumption made in operation ; - temperature drops and the heat capacity of evaporator operators! Solids content consistent with desired product quality and operating economics film evaporators provide high steam economy, defined as treatment! Are employed for the heat transfer area estimation solution would be rather straightforward, except often. Consistent with desired product quality and operating economics thermal separation, or emulsion by boiling out a solvent generally! Overcoming design problems associated with the principles of heat, and more concentrated solution remains optimum solids content with... In vapour space of the system material and energy balances with the old methods, (... A thermal separation, or emulsion by boiling out a solvent, generally water for multiple evaporators. Empirical and theoretical correlations available in tabular or graphical form tables or calculation software, as. Solids content consistent with desired product quality and operating economics a solvent, generally.... Forums › General – Cross Game Discussions › evaporator design calculations pdf file welcome Lock.

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