<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-09-20T23:14:50Z</responseDate><request verb="GetRecord" identifier="oai:cora.ucc.ie:10468/397" metadataPrefix="dim">https://cora.ucc.ie/server/oai/request</request><GetRecord><record><header><identifier>oai:cora.ucc.ie:10468/397</identifier><datestamp>2023-04-04T07:04:38Z</datestamp><setSpec>com_10468_388</setSpec><setSpec>com_10468_5</setSpec><setSpec>com_10468_1</setSpec><setSpec>com_10468_347</setSpec><setSpec>col_10468_389</setSpec><setSpec>col_10468_140</setSpec><setSpec>col_10468_375</setSpec></header><metadata><dim:dim xmlns:dim="http://www.dspace.org/xmlns/dspace/dim" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:doc="http://www.lyncode.com/xoai" xsi:schemaLocation="http://www.dspace.org/xmlns/dspace/dim http://www.dspace.org/schema/dim.xsd">
   <dim:field mdschema="dc" element="contributor" qualifier="advisor">Byrne, Edmond P.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="author">Pathare, Pankaj B.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="funder" lang="en">Department of Agriculture, Fisheries and Food, Ireland</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="accessioned">2011-08-31T11:34:00Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="available">2011-08-31T11:34:00Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="issued">2010-07</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="submitted">2010-10-07</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="abstract" lang="en">This study has considered the optimisation of granola breakfast cereal manufacturing&#xd;
processes by wet granulation and pneumatic conveying. Granola is an aggregated&#xd;
food product used as a breakfast cereal and in cereal bars. Processing of granola&#xd;
involves mixing the dry ingredients (typically oats, nuts, etc.) followed by the&#xd;
addition of a binder which can contain honey, water and/or oil.&#xd;
In this work, the design and operation of two parallel wet granulation processes to&#xd;
produce aggregate granola products were incorporated:&#xd;
a) a high shear mixing granulation process followed by drying/toasting in an&#xd;
oven.&#xd;
b) a continuous fluidised bed followed by drying/toasting in an oven.&#xd;
In high shear granulation the influence of process parameters on key granule&#xd;
aggregate quality attributes such as granule size distribution and textural properties&#xd;
of granola were investigated. The experimental results show that the impeller&#xd;
rotational speed is the single most important process parameter which influences&#xd;
granola physical and textural properties. After that binder addition rate and wet&#xd;
massing time also show significant impacts on granule properties. Increasing the&#xd;
impeller speed and wet massing time increases the median granule size while also&#xd;
presenting a positive correlation with density. The combination of high impeller&#xd;
speed and low binder addition rate resulted in granules with the highest levels of&#xd;
hardness and crispness.&#xd;
In the fluidised bed granulation process the effect of nozzle air pressure and binder&#xd;
spray rate on key aggregate quality attributes were studied. The experimental results show that a decrease in nozzle air pressure leads to larger in mean granule size. The&#xd;
combination of lowest nozzle air pressure and lowest binder spray rate results in&#xd;
granules with the highest levels of hardness and crispness. Overall, the high shear&#xd;
granulation process led to larger, denser, less porous and stronger (less likely to&#xd;
break) aggregates than the fluidised bed process.&#xd;
The study also examined the particle breakage of granola during pneumatic&#xd;
conveying produced by both the high shear granulation and the fluidised bed&#xd;
granulation process. Products were pneumatically conveyed in a purpose built&#xd;
conveying rig designed to mimic product conveying and packaging. Three different&#xd;
conveying rig configurations were employed; a straight pipe, a rig consisting two 45°&#xd;
bends and one with 90° bend. Particle breakage increases with applied pressure drop,&#xd;
and a 90° bend pipe results in more attrition for all conveying velocities relative to&#xd;
other pipe geometry. Additionally for the granules produced in the high shear&#xd;
granulator; those produced at the highest impeller speed, while being the largest also&#xd;
have the lowest levels of proportional breakage while smaller granules produced at&#xd;
the lowest impeller speed have the highest levels of breakage. This effect clearly&#xd;
shows the importance of shear history (during granule production) on breakage&#xd;
during subsequent processing. In terms of the fluidised bed granulation, there was no&#xd;
single operating parameter that was deemed to have a significant effect on breakage&#xd;
during subsequent conveying.&#xd;
Finally, a simple power law breakage model based on process input parameters was&#xd;
developed for both manufacturing processes. It was found suitable for predicting the&#xd;
breakage of granola breakfast cereal at various applied air velocities using a number&#xd;
of pipe configurations, taking into account shear histories.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="sponsorship" lang="en">Department of Agriculture, Fisheries and Food, Ireland (FIRM)</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="status" lang="en">Not peer reviewed</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="version" lang="en">Accepted Version</dim:field>
   <dim:field mdschema="dc" element="format" qualifier="mimetype" lang="en">application/pdf</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="citation" lang="en">Pathare, P.B., 2010. Optimisation of granola breakfast cereal manufacturing process by wet granulation and pneumatic conveying. PhD Thesis, University College Cork.</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="uri">https://hdl.handle.net/10468/397</dim:field>
   <dim:field mdschema="dc" element="language" qualifier="iso" lang="en">en</dim:field>
   <dim:field mdschema="dc" element="publisher" lang="en">University College Cork</dim:field>
   <dim:field mdschema="dc" element="relation" qualifier="uri">http://library.ucc.ie/record=b2027070~S0</dim:field>
   <dim:field mdschema="dc" element="rights" lang="en">© 2010, Pankaj B. Pathare</dim:field>
   <dim:field mdschema="dc" element="rights" qualifier="uri" lang="en">http://creativecommons.org/licenses/by-nc-nd/3.0/</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en">Granola breakfast cereal</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en">High shear granulation</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en">Fluidised bed granulation</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en">Texture properties</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en">Pneumatic conveying</dim:field>
   <dim:field mdschema="dc" element="subject" qualifier="lcsh" lang="en">Cereal products</dim:field>
   <dim:field mdschema="dc" element="subject" qualifier="lcsh" lang="en">Granulation</dim:field>
   <dim:field mdschema="dc" element="subject" qualifier="lcsh" lang="en">Food texture</dim:field>
   <dim:field mdschema="dc" element="subject" qualifier="lcsh" lang="en">Food processing machinery</dim:field>
   <dim:field mdschema="dc" element="subject" qualifier="lcsh" lang="en">Pneumatic-tube transportation</dim:field>
   <dim:field mdschema="dc" element="title" lang="en">Optimisation of granola breakfast cereal manufacturing process by wet granulation and pneumatic conveying</dim:field>
   <dim:field mdschema="dc" element="type" lang="en">Doctoral thesis</dim:field>
   <dim:field mdschema="dc" element="type" qualifier="qualificationlevel" lang="en">Doctoral</dim:field>
   <dim:field mdschema="dc" element="type" qualifier="qualificationname" lang="en">PhD (Process &amp;amp; Chemical Engineering)</dim:field>info:eu-repo/semantics/openAccess</dim:dim></metadata></record></GetRecord></OAI-PMH>