Analysis of Process Parameters for Optimization of Plastic Extrusion in Pipe Manufacturing

Total Page:16

File Type:pdf, Size:1020Kb

Analysis of Process Parameters for Optimization of Plastic Extrusion in Pipe Manufacturing Mr. Sandip S. Gadekaret al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 5, ( Part -1) May 2015, pp.71-74 RESEARCH ARTICLE OPEN ACCESS Analysis of Process Parameters for Optimization of Plastic Extrusion in Pipe Manufacturing Mr. Sandip S. Gadekar1, Prof.Javed G. Khan2, Dr. R. S. Dalu3 1ME Student SSGMCE Shegaon, SGBAU, Amravati 2 Assistant Professor Dept of Mech, Engg. SSGMCE Shegaon 3Professor Dept of Mechanical Engineering, Government college of Engineering Amaravati, SGBA University Abstract The objective of this paper is to study the defects in the plastic pipe, to optimize the plastic pipe manufacturing process. It is very essential to learn the process parameter and the defect in the plastic pipe manufacturing process to optimize it. For the optimization Taguchi techniques is used in this paper. For the research work Shivraj HY-Tech Drip Irrigation pipe manufacturing, Company was selected. This paper is specifically design for the optimization in the current process. The experiment was analyzed using commercial Minitab16 software, interpretation has made, and optimized factor settings were chosen. After prediction of result the quality loss is calculated and it is compare with before implementation of DOE. The research works has improves the Production, quality and optimizes the process. Key word: Taguchi method, Design of experiment, Taguchi loss function, orthogonal array. I. INTRODUCTION Take off Speed Extrusion is any process in which a material is Temperatures force through a shaped orifice, with the material Vacuum Pressure solidifying to produce a continuous length of constant And Relative speed of auxiliary cross section. Squeezing toothpaste from a tube is a familiar example. In plastic extrusion, thermoplastic III. Defects in the plastic pipe Making were softened by heating prior to extrusion and, for process the shape to be held; the thermoplastics must be The common failure or defect which are quickly chilled and, usually, supported while cooling. normally occurring in plastic extrusion process are Some large extruders in polymerization plants are fed due to three main causes are part and mold design, hot melts, so their main duty is generating enough material selection, and processing. In many cases, the pressure to force the melt through spider die. In most failures occur during the processing and these failures extrusion operations, however, the plastics arrive as cause some defects that canfound in extruded part. powders or pellets at room temperature, and the Following are the defects found in the extrusion extrusion process must melt the plastic and process homogenize it before it enters the die. Therefore, Uneven Wall thickness heating and melting the feedstock, converting it from Centering problem(off-center) a cold solid to a hot viscous liquid, accounts for about Diameter variation 93% of the energy required. The work done in Crack pumping the melt through the die is only 5-10% of Discontinuity in drilling the total [1]. Rough surface finishing In the extrusion product the defect are become during II. Importantprocess parameters in the production due to poor understanding of the extrusion process- processing method, use of inadequate or machines, Effective extrusion process requires that the lack of trained staff Machine Break Down, and machine and tool operating in well conditions. This inappropriate working environments. requires control over the process parameters such as temperature, pressure, machine speed, and the IV. Need of the optimization of the relative speeds of the auxiliary [1]. As these process parameters. manufacturing processes involve steady state Plastic pipe extrusion process is the most widely conditions, any action that can stabilize any pipe manufacturing process use in the industry. In the parameter or condition is beneficial to the process extrusion process as discuss above the various defects [2]. Mainly the plastic pipe extrusion process is are frequently occurs and hampers the productivity. If depend on the following parameters we need to enhance the production rate, it is very www.ijera.com w 71|P a g e Mr. Sandip S. Gadekaret al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 5, ( Part -1) May 2015, pp.71-74 essential to optimize the process parameters and Following are the Taguchi method steps: improve the productivity; following are the reason to optimize the process parameters Improve the product quality production rate Minimize the variations. Design and develop the product for robust component. V. Methodology for research work To optimize the process parameters in extrusion process following methodology followed. Select the plastic pipe manufacturing industry. Figure 1: Taguchi’s method Collection of data regarding the various defects in extrusion process. a)Identification of influencing factors Finding out the parameter responsible for the Take off Speed defects and their causes. Temperatures Apply the Taguchi’s method Vacuum Pressure Predict the process parameters’, which is Relative speed of auxiliary optimized.Compare the data with previous b)Level Selection for factor VI. Planning of experiment HDPE Pipe ø14smm/1.0. 6.1 Selection of industry Control factors L e v e l For research work Shivraj HY-Tech Drip (Temperature zones Irrigation Company was selected this company is in ͦC , Take-off situated in MIDC Khamgaon, in Buldhana district of speed in Maharashtra state in India. Uni m/min) 1 2 3 t 6.2 Collection of data m/ Take-off speed 18 20 22 Table1 Data collection for1-month observation min Frequency of Temperature1 in ͦc 172 178 180 S.No Type of quality defects defect Temperature2 in ͦc 169 173 165 1 Uneven Wall thickness (A) 3000 Centering problem(off- 2 300 c) Selection of orthogonal array center) (B) The choice of a suitable OA design is 3 Diameter variation (C) 2400 critical for the success of experiment design and this 4 Crack (D) 900 depends upon number of process parameters and their 5 Discontinuity in drilling (E) 1200 level. In this, work L9 OA was select with the help of 6 Rough surface finishing (F) 600 Minitab-15 software and following calculations ware 7 Total 8400 adopted. 6.3 Data analysis- d) S/N Calculation From the above observation, it is conclude that SNRA MEAN the uneven wall thickness is most important 51.1228 13.9955 parameter, which affect the process and we 38.5829 13.9955 concentrating on the same in this paper 35.0237 14.0350 6.4 Apply Taguchi Method 39.9747 14.1010 6.4.1 Taguchi technique for optimization: 65.1097 14.0075 Taguchi and Konashi developed Taguchi 36.0364 14.0680 techniques [2]; these techniques have been utilized 37.4455 14.1220 widely in engineering analysis to optimize the performance characteristics within the combination 39.0221 14.0895 of design parameters. Taguchi technique is also 35.2488 14.1580 optimization power tool for the design of quality system. It introduced an integrated that is simple and Table 2 Mean response and S/N ratio analysis efficient to find the optimum range of design for Flexible conduit (F/C∅ퟏ4풎풎) quality performance, and computational cost[3]. www.ijera.com w 72|P a g e Mr. Sandip S. Gadekaret al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 5, Issue 5, ( Part -1) May 2015, pp.71-74 For this product L9rthogonal array is chosen and Graph no.1 the all factors main effect plot for the Taguchi’s design is used. The mean response value means and Signal to noise ratio is shown in the and S/N response value is shown in the table figures below for the product F/C14mm Table-3 Table 3Response Table for Means of F/C ∅ퟏ4퐦퐦 Take off Level Temp1 Temp2 Speed 1 14.06 14.07 14.05 2 14.01 14.03 14.05 Graph 1(a)data means for means (b) data means 3 14.12 14.09 14.08 for SN ratio Delta 0.11 0.06 0.03 Rank 1 2 3 The target value required to be produced 14mm and the mean response graph above sows that on the Table 4 take off speed 2 setting 20m/min, temperature 2 Analysis of variance for means of F/C 14mm setting 178, temperature 3 setting 169 produce the Sourc DF Seq SS Adj Adj MS product with the value close to target value. But to F P e SS select setting its effect on the S/N ratio should be Take- 0.0197 0.0197 0.00988 27. 0.03 considered. The response S/N ratio is required to be 2 Off 66 66 3 97 5 large or should not be significantly minimized for Temp1Speed 0.0051 0.0051 0.00256 7.2 0.12 any type of design of experiment analysis, and from 2 19 19 0 4 1 the response S/N ration above figure is Take off Temp2 0.0020 0.0020 2.9 0.25 speed 1 setting 18, temperature 2 setting 178, 2 0.01030 59 59 1 5 temperature 3 setting 165 makes the response S/N Residu 0.0007 0.0007 0.00035 ratio large. 2 al 07 07 3 To select optimum setting of temperature values, the setting that results in a mean response value TotalError 0.0276 8 closing to the target value and that has a large or not 51 significantly reduced S/N ratio is advised be considered. Table 5 From the analysis before and the main effects Response Table for S/N Ratio of F/C 14mm plot in the previous figures, factors and their Source DF Seq Adj Adj F P respective levels selected for this product are: SS SS MS Take off speed-------------------------18 (level 1) Take- 144.7 144.7 0.4 0.6 Temperature 2------------------------172 (level 1) Off 2 72.37 4 4 4 94 Temperature 3------------------------165 (level 1) Speed 224.5 224.5 112.2 0.6 0.5 Temp1 2 In addition, the predicted value of the response 1 1 5 8 94 parameter at these temperature settings is 0.2 0.7 Temp2 2 94.24 94.24 47.12 Mean value---------------------------14.059mm 9 77 S/N ratio value-----------------------51.84db Residual 328.9 328.9 164.4 2 Standard deviation-------------------0.0821 Error 8 8 9 792.4 Total 8 Summary of factor setting selected using the 6 design of experiment Table 6 Analysis of variance for S/N ratio of F/C Controlled Factor Unit 1,2,3 14mm Take-off speed m/min 18 (level 1) Take off Level Temp1 Temp2 Speed Temperature1 in ͦC 172 (level 1) 1 47.04 42.85 45.86 Temperature2 in ͦC 165 (level 1) 2 41.58 47.57 42.06 3 37.24 35.44 37.94 Delta 9.80 12.14 7.92 Rank 2 1 3 www.ijera.com w 73|P a g e Mr.
Recommended publications
  • Polymer Extrusion Cooling for the 21 Century
    Polymer Extrusion Cooling for the 21st Century A white paper by: Wesley J. Sipe, Mechanical Systems Manager, GAI Consultants On Behalf Of: NOVATEC, Inc. Baltimore, MD USA Considering all of the plastic produced and With these keys, required cooling times can used every day, it is surprising that very little be determined through the use of advanced is documented on the cooling process for computer models. continuous profiles of extruded shapes. The bulk of the cooling process is The challenge to this methodology is in accomplished through the application of obtaining accurate thermal conductivity and “rules of thumb” learned and used by heat capacity of polymer compounds for use cooling tank manufacturers, and through in predicting thermal response. Since there trial and error methods of individual are literally thousands of compounds that processors. In spite of the desirability of are used in polymer extrusion, this paper processors to minimize space and elapsed concentrates on only six commonly used: time required to effectively cool profiles, the Polyethylene (PE) cooling process remains a “black art” as no Polypropylene (PP) tools exist that will accurately predict the Polycarbonate (PC) time response of cooling plastics with Polystyrene (PS) liquids. This is remarkable in itself because the cooling puzzle can be solved through Poly Vinyl Chloride (PVC) the simplification of the transient heat Acrylonitrile Butadiene Styrene transfer equation for the materials involved. (ABS). Even more remarkable is that through the All of the analyses described in this paper use of powerful personal computers, the assume isotropic forms with temperature process can be modeled and a solution dependent properties.
    [Show full text]
  • Extrusion Foaming of Bioplastics for Lightweight Structure in Food Packaging
    EXTRUSION FOAMING OF BIOPLASTICS FOR LIGHTWEIGHT STRUCTURE IN FOOD PACKAGING A thesis submitted for the degree of Doctor of Philosophy by Sitthi Duangphet School of Engineering and Design Brunel University December 2012 i Abstract This thesis reports the systematic approaches to overcome the key drawbacks of the pure PHBV, namely low crystallisation rate, tensile strength, ductility, melt viscosity, thermal stability and high materials cost. The physical, mechanical, thermal, and rheological properties of the pure PHBV were studied systematically first to lay a solid foundation for formulation development. The influence of blending with other biopolymers, inclusion of filler, and chain extender additives in terms of mechanical properties, rheology, thermal decomposition and crystallization kinetics were then followed. Creating lightweight structures by foaming is considered to be one of the effective ways to reduce material consumption, hence the reduction of density and morphology of PHBV-based foams using extrusion foaming technique were studied comprehensively in terms of extrusion conditions (temperature profiles, screw speed and material feeding rate) and the blowing agent content. The material cost reduction was achieved by adding low-cost filler (e.g. CaCO3) and reduction of density by foaming. The thermal instability was enhanced by incorporation of chain extender (e.g. Joncryl) and blending with a high thermal stability biopolymer (e.g. PBAT). The polymer blend also improved the ductility. Adding nucleation agent enhanced the crystallization rate to reduce stickiness of extruded sheet. The final formulation (PHBV/PBAT/CaCO3 composite) was successfully extruded into high quality sheet and thermoformed to produce prototype trays in an industrial scale trial. The effect of the extrusion conditions (temperature profiles, screw speed and material feeding rate) and the blowing agent content are correlated to the density reduction of the foams.
    [Show full text]
  • Plastic Extrusion
    The Magazine for ENERGY EFFICIENCY in Compressed Air, Pneumatics, Blower and Vacuum Systems April 2013 Plastic Extrusion 10 Plastic Extruder Saves $116,000 in Energy Costs 16 MGM Industries Reduces Chilled Water Requirements with Dry Vacuum Pumps 22 Air Audit of a Powder Coating System 28 Filtration Improves Pneumatic Performance REMOTE AIR COMPRESSOR SENSING 36 Atlas Dry Air Ad 8.375 x 10.875:Layout 2 3/5/13 1:33 PM Page 1 Clear the way for quality air 140 years of history, and the present is yours Optimizing air supply quality is a way of life at Atlas Copco. Our dryers, aftercoolers, filters and oil-mist eliminators help ensure that your air is always clean, dry and ready for the summer heat. And it doesn’t stop with quality air because the right air system components also save energy. Atlas Copco knows you have challenging targets to reduce energy costs. We know because we face those targets, too! With 14 production facilities in the United States and dozens more globally, we never stop looking for ways to help our manufacturing teams, and yours, save energy and increase productivity. In 2013 Atlas Copco celebrates our 140th birthday. To celebrate this key milestone we are offering a series of gifts: starting with simple air studies for free. We’ll log your plant’s actual air usage, show you ways to save money and compute the payback on any new investments. Sign up now and you’ll receive a limited edition anniversary baseball cap. Register at www.atlascopco.us/mboxusa or call 866-688-9611.
    [Show full text]
  • Simulation of Extrusion of High Density Polyethylene Tubes
    MATEC Web of Conferences 112, 04004 (2017) DOI: 10.1051/matecconf/20171120400 4 IManE&E 2017 Simulation of extrusion of high density polyethylene tubes Antonios Koutelieris1, Kyriaki Kioupi1, Onoufrios Haralampous1, Konstantinos Kitsakis1,2,*, Nikolaos Vaxevanidis3, and John Kechagias1 1Technological Educational Institute of Thessaly, Mechanical Engineering Department, 41110 Larissa, Greece 2University of Western Macedonia, Mechanical Engineering Department, 50100 Kozani, Greece 3School of Pedagogical and Technological Education, Mechanical Engineering Educators Department, 14121 N. Heraklion Attikis, Greece Abstract. The production of extruded polyethylene films rods, tubes and pipes is a typical industrial process that has been extensively investigated over many years. In this study the extrusion of High Density Polyethylene (HDPE) tubes was simulated by using the 3D finite element simulation software StarCCM+®. The simulation was applied in order to examine the influence of design and operational parameters on the characteristics and the soundness of the tube and for optimizing the overall quality of the product. Two alternative die configurations were studied; one with a four inputs head and the other with an eight inputs head. From the results obtained it is concluded that extrusion with the eight inputs head die design results in better overall pipe quality; this design was implemented successfully in an industrial production line. 1 Introduction High-density polyethylene (HDPE) tubes are typically used in many applications such as to convey potable water, waste water, chemicals, etc. HDPE has high strength, toughness, durability and resistance to chemicals. In order to manufacture solid wall pipes the following steps should be followed: heat, melt, mix, and convey the raw material into a mold to achieve the final form.
    [Show full text]
  • Processing of Bioplastics – a Guideline – Photo: Fraunhofer IAP Fraunhofer Photo: Photo: Fraunhofer IAP Fraunhofer Photo: IAP Fraunhofer Photo: Ifbb Photo
    Photo: Fraunhofer IAP Photo: Fraunhofer IAP Processing ofBioplastics Processing Photo: Fraunhofer IAP – aguideline Photo: IfBB Preface For more than 20 years, the Federal Ministry of Food and Agriculture (BMEL) has been promoting, via its project co-ordination agency FNR (Fachagentur Nachwachsende Rohstoffe e. V.), the research and development of energy and products based on renewable raw materials. Bioplastics have always been a major priority in this context. Their promotion has, however, never been closer to real practice than with the collaborative project “Kompetenznetzwerk zur Verarbeitung von Biokunststoffen” (Competence network for the processing of bioplastics), which has been supported financially by the BMEL since the beginning of 2013. With the establishment of four regional centres of excellence for the material-related processing of bio-based polymers, research funding has left the laboratories and placed itself at the side of the user. The goal of the project is, on the one hand, to accelerate the transfer of know-how from research and development to the processors of bioplastics and, on the other hand, to address and resolve the suggestions, questions and problems of, in particular, the many medium-sized companies who genuinely want to pursue innovative approaches. In the past three years, the four alliance partners have moved much closer to this goal. An important result of this work is the brochure which you are holding in your hands today. The brochure provides an overview of the data compiled over the last three years concerning the processing of bioplastics. The brochure primarily represents a showcase which will encourage you to look deeper, as the specific technical data concerning the materials and the processing can be found on the Internet in the corresponding database.
    [Show full text]
  • Food Packaging Technology
    FOOD PACKAGING TECHNOLOGY Edited by RICHARD COLES Consultant in Food Packaging, London DEREK MCDOWELL Head of Supply and Packaging Division Loughry College, Northern Ireland and MARK J. KIRWAN Consultant in Packaging Technology London Blackwell Publishing © 2003 by Blackwell Publishing Ltd Trademark Notice: Product or corporate names may be trademarks or registered Editorial Offices: trademarks, and are used only for identification 9600 Garsington Road, Oxford OX4 2DQ and explanation, without intent to infringe. Tel: +44 (0) 1865 776868 108 Cowley Road, Oxford OX4 1JF, UK First published 2003 Tel: +44 (0) 1865 791100 Blackwell Munksgaard, 1 Rosenørns Allè, Library of Congress Cataloging in P.O. Box 227, DK-1502 Copenhagen V, Publication Data Denmark A catalog record for this title is available Tel: +45 77 33 33 33 from the Library of Congress Blackwell Publishing Asia Pty Ltd, 550 Swanston Street, Carlton South, British Library Cataloguing in Victoria 3053, Australia Publication Data Tel: +61 (0)3 9347 0300 A catalogue record for this title is available Blackwell Publishing, 10 rue Casimir from the British Library Delavigne, 75006 Paris, France ISBN 1–84127–221–3 Tel: +33 1 53 10 33 10 Originated as Sheffield Academic Press Published in the USA and Canada (only) by Set in 10.5/12pt Times CRC Press LLC by Integra Software Services Pvt Ltd, 2000 Corporate Blvd., N.W. Pondicherry, India Boca Raton, FL 33431, USA Printed and bound in Great Britain, Orders from the USA and Canada (only) to using acid-free paper by CRC Press LLC MPG Books Ltd, Bodmin, Cornwall USA and Canada only: For further information on ISBN 0–8493–9788–X Blackwell Publishing, visit our website: The right of the Author to be identified as the www.blackwellpublishing.com Author of this Work has been asserted in accordance with the Copyright, Designs and Patents Act 1988.
    [Show full text]
  • Impact of Extrusion Process on Product Quality
    International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 01 | Jan 2019 www.irjet.net p-ISSN: 2395-0072 IMPACT OF EXTRUSION PROCESS ON PRODUCT QUALITY Sunil Kumar1, P.S Rao2 1ME Scholar (171222-Modular), Mechanical Engineering, NITTTR CHANDIGARH 2Associate Professor, Mechanical Engineering, NITTTR CHANDIGARH -------------------------------------------------------------------------***------------------------------------------------------------------------ ABSTRACT - This paper is based on impact analysis of extrusion process on quality of product. Approximately large number of manufacturers experienced a problem in product quality in established extrusion pipe manufacturing process to compete the customer demand. To ensure product quality in present extrusion pipe manufacturing process, it is compulsory to identify, control, and regular monitoring of all quality parameters to ensure product quality. Some of the important parameters are based on the condition of equipment used in process, operating conditions, temperatures, pressures, dies quality, and used materials. So many problems faced by the manufacturers to minimize defect in the final products which directly affect the cost of product as well as product life. The purpose of this paper is to focus to analyze the various defects in the extrusion process, to access its impact on the product quality and to suggest the mitigation & remedies for the improvement of extrusion process for better product quality and life. Keywords: Extrusion process, Defects in plastic pipe, Impact of defect, Product quality INTRODUCTION Manufacturing of plastic products in India started 60-62 years ago with the countries. The Indian plastics market is comprised of around 25,000 companies and employs 3 million people. The domestic capacity for plastic production was more than 6.72m tonnes in 2016-17.
    [Show full text]
  • 2017 ANTEC Extrusion Program New This Year at ANTEC ...Ask the Experts
    SPRING 2017 A Message From the Chair VOLUME 42, ISSUE 1 The past year and likely the next few years will be characterized by many changes for the Extrusion Division and the SPE as a whole. Many long time Board My Plastics Life 3 Members either are retiring, or will be retiring soon, so the torch must be effectively passed to the younger generation. As such, many long term paradigms and methods of operation may be challenged: 1.What are the goals of the Extrusion Division as a whole going forward? ANTEC Extrusion 11 2.What does the membership expect and how can we Program increase membership and participation in the SPE and the Extrusion Division? 3.How can we make membership in the SPE and participation on the Board a positive and rewarding experience? 4.What role will ANTEC play in the future and will it Optimize Feeding in 14 survive, and if so, how can we change the venue to Compounding attract more of the membership and be more cost effective? It will not be possible to expand on all of these points in this message, but I would like to comment on a new strategy being directed at ANTEC this year. In the past few years the number of submitted technical papers has dropped significantly. While this presents a challenge, it also offers an Tech Tips: Identifying 15 opportunity to restructure our ANTEC offering. While there will always be a forum at ANTEC for new Screw Wear technology and an open invitation for the membership to submit technical papers, it is imperative that we adjust the offering to cover a broader range of information relevant to the needs of the membership.
    [Show full text]
  • Comparison and Analysis of Biobased/Biodegradable and Petrochemical Cutlery Flexibility" (2011)
    Iowa State University Capstones, Theses and Graduate Theses and Dissertations Dissertations 2011 Comparison and analysis of biobased/ biodegradable and petrochemical cutlery flexibility Brian J. Demmer Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/etd Part of the Bioresource and Agricultural Engineering Commons Recommended Citation Demmer, Brian J., "Comparison and analysis of biobased/biodegradable and petrochemical cutlery flexibility" (2011). Graduate Theses and Dissertations. 12136. https://lib.dr.iastate.edu/etd/12136 This Thesis is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Graduate Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. Comparison and analysis of biobased/biodegradable and petrochemical cutlery flexibility by Brian John Demmer A thesis submitted to the graduate faculty in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE Major: Industrial & Agricultural Technology Program of Study Committee: David Grewell, Major Professor Steven Freeman Carolyn Heising Iowa State University Ames, Iowa 2011 Copyright © Brian John Demmer, 2011. All rights reserved. ii DEDICATION This paper is dedicated to my loving family and friends iii TABLE OF CONTENTS LIST OF TABLES ....................................................................................................................v
    [Show full text]
  • PROJECT REPORT of BIODEGRADABLE PLASTIC
    PROJECT REPORT Of BIODEGRADABLE PLASTIC BAGS (PLA BASED) PURPOSE OF THE DOCUMENT This particular pre-feasibility is regarding Biodegradable Plastic Bags (PLA Based). The objective of the pre-feasibility report is primarily to facilitate potential entrepreneurs in project identification for investment and in order to serve his objective; the document covers various aspects of the project concept development, start-up, marketing, finance and management. [We can modify the project capacity and project cost as per your requirement. We can also prepare project report on any subject as per your requirement.] M/s Institute of Industrial Development A Unit of M/s SAMADHAN Samiti KVIC Pavilion, Gandhi Darshan, Raj Ghat, New Delhi 110002 Head office: Samadhan Tower, 27/1/B, Gokhle Marg, Lucknow-226001 Website: www.iid.org.in Email: [email protected] BIODEGRDABLE PLATSIC BAGS (PLA BASED) MANUFACTURING 1. INTRODUCTION The term “Biodegradable” refers to anything or substances that can be degraded by the natural forces and micro-organisms and Bio-degradable plastics refer to those plastics that can be decomposed by the micro-organisms and also natural factors such as rain, sunlight, etc. Hence these bags will not pose to be a threat to the environment. Plastic bags can be made “Oxo-biodegradable” by manufacturing theme from the normal polyethylene or the polypropylene and then incorporating an additive that can cause them to degrade and then biodegradation of the polymer by oxidation. Fig.: Biodegradable Plastic Bags and PLA pellets The global production capacity of the biodegradable plastic bags reached around 1.17 million tons in 2019. Polylactic Acid (PLA) based is probably the most well-known biodegradable plastic but besides that there are about 20 groups of biodegradable plastic polymers.
    [Show full text]
  • How Plastic Extrusion Works
    32 Park Street PO Box 40-924 Upper Hutt How Plastic Extrusion Works In the extrusion process, plastic resin beads are fed into a hopper, along with any colours or additives. Heat is applied and the resin then feeds the beads down through onto a large spinning screw within a horizontal barrel. The beads pass through the barrel on the screw while being heated to the melting temperature specific to that type of plastic. By the time it meets the end of the screw the plastic is thoroughly mixed and has a consistency like thick bubble gum. At the end of the screw the extruded plastic flows across a screen and a breaker plate which serves two functions. The screen removes the containments or inconsistencies in the plastic, and the breaker plate changes the motion of the plastic from rotational to longitudinal. It’s now ready for the die. The continuous flow of molten plastic is forced through the die, and the plastic is then cooled. Depending on the shape of the die opening many different parts can be made including tube, piping and profiles. Although it is possible, and sometimes necessary, to shape the plastic flow downstream after it leaves the die, it is the shape of the die opening that determines the shape of the finished product. While the die determines the shape of the plastic flow, many different methods are used downstream to make different parts. The technique of making pipe differs from that of making profiles. In some instances a cooling water bath may be used while other times air jets, water sprays, fans, vacuum boxes or just air in the room may be used.
    [Show full text]
  • Environmental Payback Periods of Reusable Alternatives to Single-Use Plastic Kitchenware Products
    Environmental Payback Periods of Reusable Alternatives to Single-Use Plastic Kitchenware Products By: Hannah Fetner A thesis submitted in partial fulfillment of the requirements for the degree of Master of Science (Natural Resources and Environment) in the University of Michigan 04/2021 Thesis Committee: Professor Shelie A Miller, Chair Professor Gregory Keoleian ii Abstract Many consumers are transitioning away from single-use plastic products and turning to reusable alternatives. Oftentimes this change is being made with the assumption that these alternatives have fewer environmental impacts; however, reusable products are frequently made from more environmentally-intensive materials and have use phase impacts. This study used LCA to examine the GWP, water consumption and primary nonrenewable energy use associated with reusable alternatives for single-use plastic kitchenware products, and determined environmental payback periods. Payback periods are calculated for each reusable alternative and defined as the number of times a consumer must re-use an alternative in order for the environmental impact per use to be equivalent to the environmental impact for the single-use product. The research explored the sensitivity of the results to different consumer washing and reuse behaviors, as well as local conditions such as overall transportation distances and the carbon intensity of different electricity grids. Product types studied included straws (4 reusable, 2 single-use), sandwich storage (2 reusable, 3 single-use), coffee cups (3 reusable, 2 single-use) and forks (1 single-use, 3 reusable). Environmental impacts associated with the reusable alternatives were highly dependent on the use phase due to dishwashing, making payback period sensitive to washing frequency and method, and for GWP, carbon intensity of the energy grid (used for water heating).
    [Show full text]