<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.3 20210610//EN" "https://jats.nlm.nih.gov/publishing/1.3/JATS-journalpublishing1-3.dtd"><article xml:lang="en" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:ali="http://www.niso.org/schemas/ali/1.0/" dtd-version="1.3" article-type="research-article"><front><journal-meta><journal-id journal-id-type="issn">2354-886X</journal-id><journal-title-group><journal-title>Jurnal Pengolahan Hasil Perikanan Indonesia</journal-title><abbrev-journal-title>JPHPI</abbrev-journal-title></journal-title-group><issn pub-type="epub">2354-886X</issn><issn pub-type="ppub">2303-2111</issn><publisher><publisher-name>Department of Aquatic Product Technology IPB University in collaboration with Masyarakat Pengolahan Hasil Perikanan Indonesia (MPHPI)</publisher-name><publisher-loc>Indonesia</publisher-loc></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.17844/65efk717</article-id><article-categories></article-categories><title-group><article-title>Mechanistic integration of thermodynamic quality during transient air blast freezing of export-grade shrimp</article-title><subtitle>Integrasi mekanistik termodinamika-kualitas selama air blast freezing transien pada udang kelas ekspor</subtitle></title-group><contrib-group><contrib contrib-type="author"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0008-4035-7561</contrib-id><name><surname>Nugroho</surname><given-names>Faizin Adi</given-names></name><address><country country="ID">Indonesia</country><email>faizin.adi89@gmail.com</email></address><xref ref-type="aff" rid="AFF-1"></xref><xref ref-type="corresp" rid="cor-0"></xref></contrib><contrib contrib-type="author"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-0434-7269</contrib-id><name><surname>Krisnafi</surname><given-names>Yaser</given-names></name><address><country country="ID">Indonesia</country><email>yaser_bunda@yahoo.com</email></address><xref ref-type="aff" rid="AFF-1"></xref></contrib><contrib contrib-type="author"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0008-5164-1891</contrib-id><name><surname>Khikmawati</surname><given-names>Liya Tri</given-names></name><address><country country="ID">Indonesia</country><email>liya.3khikmawati@gmail.com</email></address><xref ref-type="aff" rid="AFF-1"></xref></contrib><contrib contrib-type="author"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0003-1624-4782</contrib-id><name><surname>Lailatussifa</surname><given-names>RR. Radipta</given-names></name><address><country country="ID">Indonesia</country><email>rr.radipta@gmail.com</email></address><xref ref-type="aff" rid="AFF-2"></xref></contrib><contrib contrib-type="author"><name><surname>Astiana</surname><given-names>Ika</given-names></name><address><country country="ID">Indonesia</country><email>astianaika90@gmail.com</email></address><xref ref-type="aff" rid="AFF-3"></xref></contrib><contrib contrib-type="author"><contrib-id contrib-id-type="orcid">https://orcid.org/0009-0006-8776-7651</contrib-id><name><surname>Pratiwi</surname><given-names>Citra Zaskia</given-names></name><address><country country="ID">Indonesia</country><email>citra.pratiwi@kkp.go.id</email></address><xref ref-type="aff" rid="AFF-4"></xref></contrib></contrib-group><aff id="AFF-1"><institution content-type="dept">Department of Fisheries Mechanization</institution><institution-wrap><institution>Sidoarjo Marine and Fisheries Polytechnic</institution></institution-wrap><addr-line>Buncitan st., Sedati,</addr-line><city>Sidoarjo</city><country country="ID">Indonesia</country></aff><aff id="AFF-2"><institution content-type="dept">Fishery Product Processing</institution><institution-wrap><institution>Sidoarjo Marine and Fisheries Polytechnic</institution></institution-wrap><addr-line>Buncitan st., Sedati,</addr-line><city>Sidoarjo,</city><country country="ID">Indonesia</country></aff><aff id="AFF-3"><institution content-type="dept">Marine Product Processing</institution><institution-wrap><institution>Jembrana Marine and Fisheries Polytechnic</institution></institution-wrap><addr-line>Pengambengan st., Negara,</addr-line><city>Jembrana</city><country country="ID">Indonesia</country></aff><aff id="AFF-4"><institution content-type="dept">Fisheries Mechanization</institution><institution-wrap><institution>Sidoarjo Marine and Fisheries Polytechnic</institution></institution-wrap><addr-line>Buncitan st., Sedati,</addr-line><city>Sidoarjo</city><country country="ID">Indonesia</country></aff><author-notes><corresp id="cor-0">Corresponding author: Faizin Adi  Nugroho. Email: <email>faizin.adi89@gmail.com</email></corresp></author-notes><pub-date date-type="pub" iso-8601-date="2026-06-29" publication-format="electronic"><day>29</day><month>06</month><year>2026</year></pub-date><pub-date date-type="collection" iso-8601-date="2026-06-29" publication-format="electronic"><day>29</day><month>06</month><year>2026</year></pub-date><volume>29</volume><issue>6</issue><issue-title>Jurnal Pengolahan Hasil Perikanan Indonesia 29(6)</issue-title><fpage>562–581</fpage><lpage>581</lpage><history><date date-type="received" iso-8601-date="2025-11-21"><day>21</day><month>11</month><year>2025</year></date><date date-type="accepted" iso-8601-date="2026-03-13"><day>13</day><month>03</month><year>2026</year></date></history><permissions><copyright-statement>Copyright (c) 2026 Faizin Adi  Nugroho, Yaser  Krisnafi, Liya Tri  Khikmawati, RR. Radipta  Lailatussifa, Ika Astiana, Citra Zaskia  Pratiwi</copyright-statement><copyright-year>2026</copyright-year><copyright-holder>Faizin Adi  Nugroho, Yaser  Krisnafi, Liya Tri  Khikmawati, RR. Radipta  Lailatussifa, Ika Astiana, Citra Zaskia  Pratiwi</copyright-holder><license license-type="open-access" xlink:href="https://creativecommons.org/licenses/by/4.0/"><ali:license_ref xmlns:ali="http://www.niso.org/schemas/ali/1.0/">https://creativecommons.org/licenses/by/4.0/</ali:license_ref><license-p>This work is licensed under a Creative Commons Attribution 4.0 International License.Authors who publish with this journal agree to the following terms:Authors retain copyright and grant the journal right of first publication with the work simultaneously licensed under a Creative Commons Attribution License that allows others to share the work with an acknowledgement of the work's authorship and initial publication in this journal.Authors are able to enter into separate, additional contractual arrangements for the non-exclusive distribution of the journal's published version of the work (e.g., post it to an institutional repository or publish it in a book), with an acknowledgement of its initial publication in this journal.</license-p></license></permissions><self-uri xlink:href="https://journal.ipb.ac.id/jphpi/article/view/69742" xlink:title="69742"></self-uri><abstract><p>Shrimp quality is highly sensitive to freezing stability during early post-harvest handling. Although air blast freezers (ABF) are widely applied in industrial processing, the quantitative linkage between transient thermodynamic degradation and early microstructural deterioration remains insufficiently resolved. This study aims to investigate the mechanistic relationship between early-stage ABF performance decay and time-resolved shrimp quality changes during the first 6 h of freezing. An integrated experimental approach was conducted by combining in-situ measurements of airflow velocity, air-side temperature differential (ΔT), evaporator frosting mass, cooling capacity (Q), and actual coefficient of performance (COP) with laboratory analyses of ice crystal size, water-holding capacity (WHC), drip loss, texture, pH, melanosis, and TVB-N. The results demonstrate a progressive frosting accumulation (0.09-1.50 kg) that reduced airflow (4.38-2.62 m s -¹), suppressed cooling capacity (28.99-20.98 kW), and deteriorated . Frosting mass explained up to 97-98% of COP and Q variance. Sequential regression analysis confirmed a strong mechanistic pathway: COP decline significantly enlarged ice crystals (R² = 0.97), which reduced WHC (R² = 0.96) and increased drip loss (R² = 0.98). These findings indicate that transient thermodynamic instability, rather than steady-state temperature compliance alone, governs early structural degradation. The study repositions COP as a predictive upstream control parameter linking machine performance to product integrity and provides a performance-oriented framework for HACCP-integrated monitoring and early operational optimization in industrial shrimp freezing systems.</p></abstract><kwd-group><kwd>COP</kwd><kwd>frost effect</kwd><kwd>freezing temperature fluctuations</kwd><kwd>shrimp quality</kwd></kwd-group><custom-meta-group><custom-meta><meta-name>File created by JATS Editor</meta-name><meta-value>https://jatseditor.com</meta-value></custom-meta><custom-meta><meta-name>issue-created-year</meta-name><meta-value>2026</meta-value></custom-meta></custom-meta-group></article-meta></front><body><sec id="sec-1"><title>INTRODUCTION</title><p>Shrimp is a high-value fishery commodity with a continuously increasing market demand. Temperature instability during air blast freezer (ABF) operation constitutes not only a thermodynamic ineficiency but also a direct economic risk factor in shrimp export systems (<xref ref-type="bibr" rid="BIBR-44">Prambudia &amp; Sriwana, 2025</xref>). Transient temperature fluctuations accelerate microstructural damage, increase drip loss, downgrade product grading, and elevate the probability of buyer rejection, thereby reducing market prices and contractual reliability (<xref ref-type="bibr" rid="BIBR-5">Anggrahini et al., 2015</xref>; <xref ref-type="bibr" rid="BIBR-35">Lin et al., 2022</xref>). Consequently, inadequate thermal control in ABF processing translates into measurable financial losses for exporters through value depreciation, return penalties, and diminished global competitiveness (<xref ref-type="bibr" rid="BIBR-47">Samanta &amp; Imroatin, 2025</xref>). The post-harvest storage conditions and freshness of shrimp significantly determine their overall quality. Enzymatic activity, microbiological processes, and lipid oxidation can rapidly deteriorate shrimp quality, resulting in noticeable changes in color, texture, and flavor (<xref ref-type="bibr" rid="BIBR-10">Cheng et al., 2025</xref>).</p><p>Consequently, to maintain shrimp quality throughout distribution and storage, the implementation of an eficient preservation method is essential (<xref ref-type="bibr" rid="BIBR-37">Liu et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-71">Zhao et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-77">Zhu et al., 2024</xref>). Although previous studies have extensively examined shrimp freezing quality, ice crystal formation, drip loss, and energy eficiency in air blast freezer systems, the direct link between transient ABF performance degradation and early stage microstructural quality loss remains unclear. The novelty of this study lies in the integration of frost-induced thermodynamic decay, represented by airflow reduction, temperature diferential changes, and COP decline, with shrimp quality kinetics, including ice crystal enlargement, water-holding capacity reduction, drip loss, and texture degradation. Therefore, this study aimed to establish a predictive thermodynamic framework that positions COP as an upstream control parameter for maintaining structural integrity and quality consistency in export-grade frozen shrimp.</p><p>Previous studies have discussed the application of freezing technology in the fisheries industry. Research conducted by <xref ref-type="bibr" rid="BIBR-31">Klunklin et al. (2025)</xref> focused on shrimp products and revealed that rapid freezing using an air blast freezer preserved shrimp quality more efectively than slow freezing methods. In addition, <xref ref-type="bibr" rid="BIBR-14">Duan et al. (2025)</xref> and <xref ref-type="bibr" rid="BIBR-71">Zhao et al. (2024)</xref> demonstrated that both freezing rate and temperature significantly influence the quality of fishery products during storage. The application of various freezing technologies for shrimp commodities demonstrates that equipment performance plays a crucial role in preserving the structural, functional, and sensory integrity of products throughout the cold-chain storage period. <xref ref-type="bibr" rid="BIBR-21">Hermes et al. (2021)</xref> highlighted that rapidfreezing methods, such as air blast freezers (ABF), generate smaller and more uniformly distributed ice crystals, thereby minimizing tissue damage, reducing moisture loss, and mitigating protein degradation commonly observed in slow-freezing processes (<xref ref-type="bibr" rid="BIBR-52">Sun et al., 2023a</xref>).</p><p>Conversely, conventional freezing at temperatures above -20°C increases drip loss, accelerates myofibrillar denaturation, and decreases water-holding capacity during thawing and subsequent heat treatment (<xref ref-type="bibr" rid="BIBR-59">Wei et al., 2024</xref>). In this context, case-based comparisons reveal that freezer performance, characterized by freezing rate, temperature stability, and airflow management, correlates directly with the final quality attributes of shrimp, including texture, color, and nutritional retention (<xref ref-type="bibr" rid="BIBR-56">Tan et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-25">Jin et al., 2018</xref>). Overall, evidence from the literature underscores that optimizing freezing technology is not merely a technical consideration but a key determinant of the success and reliability of export-grade frozen shrimp supply chains.</p><p>Despite the extensive industrial reliance on air blast freezers (ABF) for shrimp freezing, existing studies predominantly assess end-product freshness indicators (pH, TVB-N, and microbial load) without explicitly resolving how real-time ABF operational behavior governs microstructural quality deterioration. Current literature typically evaluates air temperature, freezing time, or airflow as isolated variables, while evaporator frosting, airflow instability, and thermal non-uniformity, although frequently acknowledged, are rarely quantified and analyzed as an integrated thermodynamic system. Furthermore, prior investigations have demonstrated that temperature fluctuations and slow freezing rates exacerbate ice recrystallization and protein denaturation.</p><p>However, the direct coupling between machine eficiency metrics (COP, cooling capacity, and ΔT) and physical quality indicators, such as ice crystal size, WHC, and texture loss, remains largely unexplored. In particular, no study has systematically linked the declining COP and evaporator frosting dynamics to the early stage freezing window that governs irreversible muscle damage. Additionally, HACCP-based controls in frozen seafood operations are often implemented as procedural compliance tools rather than being validated against real thermodynamic and airflow data. This creates a critical knowledge gap in which microstructural degradation can occur under microbiologically safe conditions but remains undetected by conventional quality monitoring frameworks.</p><p>To address this deficiency, the present study evaluated the ABF holistically by assessing the cooling capacity, machine eficiency, freezing time, inlet-outlet temperature profiles, frosting efects, and airflow velocity (<xref ref-type="bibr" rid="BIBR-3">Alar et al., 2024</xref>), while contextualizing these parameters against the known mechanisms of muscle structural deterioration. This study presents a comprehensive and experimentally validated framework that integrates ABF mechanical performance with evaporator frosting behavior and time-resolved shrimp quality responses. Unlike prior studies that assess equipment and products separately, this study establishes a direct causal linkage between operational deviations within the ABF system and the physical quality deterioration of shrimp muscle, thereby redefining ABF evaluation from a machine-centered to a process product coupled perspective.</p></sec><sec id="sec-2"><title>MATERIALS AND METHODS</title><p>The design and structural parameters of the air blast freezer being studied are located in the modern processing teaching factory (TEFA), which is currently rented by PT. XYZ for freezing fishery products and processed foods from frozen fishery products before export, with the technical specifications listed in <xref ref-type="table" rid="table-1">Table 1</xref>.</p><table-wrap id="table-1"><label>Table 1</label><caption><p>Bitzer S6F-30.2Y-40P ABF technical specifications</p></caption><table><colgroup><col></col><col></col></colgroup><thead><tr><th scope="col">Parameters</th><th scope="col">Value</th></tr></thead><tbody><tr><td>Compressor type</td><td>Semi hermetic, 2 stage piston</td></tr><tr><td>Number of cylinders</td><td>6 cylinder</td></tr><tr><td>Serial number (S/N)</td><td>1600810283</td></tr><tr><td>Displacement (1450 RPM)</td><td>101.1 m3/h (LP), 50.5 m3/h (HP)</td></tr><tr><td>Motor power</td><td>30 HP/ 22 KW</td></tr><tr><td>Operating voltage</td><td>380 - 420 V (50 Hz) / 440 - 480 V (60Hz), 3 phase</td></tr><tr><td>Maximum current</td><td>53 A</td></tr><tr><td>Maximum power</td><td>30.1 KW</td></tr><tr><td>Initial current (LRA)</td><td>135/220 A (Y/YY)</td></tr><tr><td>Oil capacity</td><td>4.75 liters (BSE2 for R404A/R507A)</td></tr><tr><td>Net weight</td><td>234 Kg</td></tr><tr><td>Suction line connection</td><td>42 mm ( 1 5/8” )</td></tr><tr><td>Discharge line connection</td><td>35 mm ( 1 3/8” )</td></tr><tr><td>Maximum pressure</td><td>28 bar</td></tr><tr><td>Supported refrigerants</td><td>R404A, R507A, R448A, R449A, R22 (oil based B5.2)</td></tr></tbody></table><table-wrap-foot><p>The (ABF) system used in this study was designed based on BITZER refrigeration components to ensure stable low-temperature operation during shrimp freezing. <xref ref-type="table" rid="table-2">Table 2</xref> presents the main design specifications of the ABF unit, including its refrigeration capacity, operating conditions, and supporting components used as the basis for the performance evaluation.</p></table-wrap-foot></table-wrap><table-wrap id="table-2"><label>Table 2</label><caption><p>BITZER brand air blast freezer (ABF) design specifications</p></caption><table><colgroup><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col">No.</th><th scope="col">Data</th><th scope="col"></th><th scope="col">Capacity</th></tr></thead><tbody><tr><td></td><td></td><td>Length</td><td>3.5 m</td></tr><tr><td rowspan="2">1.</td><td rowspan="2">Dimensions</td><td>Width</td><td>2.5 m</td></tr><tr><td>Height</td><td>2.5 m</td></tr><tr><td>2.</td><td>Air blast freezer capacity</td><td></td><td>2 ton</td></tr><tr><td rowspan="2">3.</td><td rowspan="2">Polyurethane walls</td><td>Thick</td><td>150 mm</td></tr><tr><td>Room</td><td>-35°C</td></tr><tr><td rowspan="3">4.</td><td rowspan="3">Temperature</td><td>Environment</td><td>30°C</td></tr><tr><td>Evaporation</td><td>-30°C</td></tr><tr><td>Floor</td><td>10°C</td></tr><tr><td rowspan="2">5.</td><td rowspan="2">Air humidity</td><td>Room</td><td>25%</td></tr><tr><td>Environment</td><td>20%</td></tr><tr><td>6.</td><td>2 Fan</td><td></td><td>800 W</td></tr><tr><td rowspan="2">7.</td><td rowspan="2">Heater defrost</td><td>Coil</td><td>5.600 W</td></tr><tr><td>Dry tray</td><td>5.600 W</td></tr></tbody></table></table-wrap><p>The physical properties of the shrimp products were characterized to provide baseline information on product dimensions, mass, and thermal-related attributes relevant to the freezing performance analysis, as summarized in <xref ref-type="table" rid="table-3">Table 3</xref>.</p><table-wrap id="table-3"><label>Table 3</label><caption><p>Physical properties of shrimp products</p></caption><table><colgroup><col></col><col></col></colgroup><thead><tr><th scope="col">Shrimp character</th><th scope="col">Value*</th></tr></thead><tbody><tr><td>C shrimp (specific heat of fresh shrimp)</td><td>3.75 kJ/kg°C</td></tr><tr><td>C shrimp (specific heat of frozen shrimp)</td><td>1.89 kJ/kg°C</td></tr><tr><td>Average temperature</td><td>5 °C</td></tr><tr><td>Shrimp freezing point</td><td>-1.94 °C</td></tr><tr><td>Freezing point of water</td><td>0 °C</td></tr><tr><td>Latent heat of shrimp</td><td>253.5 kJ/kg°C</td></tr><tr><td>C_air= (specific heat of air)</td><td>4.18 kJ/kg°C</td></tr></tbody></table><table-wrap-foot><p>*(<xref ref-type="bibr" rid="BIBR-48">Samsi ., 2023</xref>)</p></table-wrap-foot></table-wrap><p><xref ref-type="bibr" rid="BIBR-48">et al</xref></p><sec id="sec-3"><title>ABF Test Method</title><p>Field measurements were conducted using both mechanical and digital instruments in the air-blast freezer system. The collected data included temperature and pressure variables measured at several critical points within the system at specific time intervals throughout the operational periods (<xref ref-type="bibr" rid="BIBR-21">Hermes et al., 2021</xref>). Temperature monitoring was conducted using RTD PT100 sensors (Class A, ±0.15°C accuracy) with stainless steel probes (Omron E52 Series). The air velocity inside the freezing chamber was measured using a Krisbow digital anemometer (±3% accuracy, 0.01 m/s resolution) to quantify the airflow variations associated with the development of frosting and heat transfer performance. All measurements were recorded at fixed time intervals to capture the transient thermodynamic behavior during the early freezing stage. The primary objective of this measurement was to observe the system performance, identify the patterns of temperature and pressure fluctuations, and evaluate the overall system eficiency (<xref ref-type="bibr" rid="BIBR-6">Badri et al., 2021</xref>). The analysis and evaluation included:</p><p>1.Calculate the ABF air flow rate</p><disp-formula id="equation-1"><tex-math id="math-1"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm{Q} _ {\mathrm{air}} = \mathrm{A} \times \mathrm{V} \end{document} ]]></tex-math></disp-formula><p>Q = air flow rate capacity <inline-formula><tex-math id="math-2"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \text{m}^3/_s \end{document} ]]></tex-math></inline-formula></p><p>A = cross-sectional area of air duct <inline-formula><tex-math id="math-3"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { m } ^ { 2 } \end{document} ]]></tex-math></inline-formula></p><p>V = air flow rate m/s</p><p>2.Efficiency of temperature distribution in ABF</p><disp-formula id="equation-2"><tex-math id="math-4"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \Delta t = T _ {\text { inlet }} - T _ {\text { outlet }} \end{document} ]]></tex-math></disp-formula><p><inline-formula><tex-math id="math-5"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { T _ { i n l e t } = } \end{document} ]]></tex-math></inline-formula> air temperature entering the ABF room <inline-formula><tex-math id="math-6"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ^ \circ \mathrm { C } \end{document} ]]></tex-math></inline-formula></p><p><inline-formula><tex-math id="math-7"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { T } _ { \mathrm { o u t l e t } } = \end{document} ]]></tex-math></inline-formula>outlet air temperature to the ABF room <inline-formula><tex-math id="math-8"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ^ \circ C \end{document} ]]></tex-math></inline-formula></p><p>3.Cooling capacity</p><disp-formula id="equation-3"><tex-math id="math-9"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \begin{array}{l} \mathrm {Q_ {1} = m\times C_ {p} \times\Delta t} \\ \mathrm {Q_ {2} = m\times L_ {f}} \end{array} \end{document} ]]></tex-math></disp-formula><p>Q= cooling capacity (kJ or kW)</p><p>m= frozen shrimp mass (Kg)</p><p>C = specific heat capacity of shrimp before freezing <inline-formula><tex-math id="math-10"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { ( k J / K g ) } \end{document} ]]></tex-math></inline-formula></p><p>∆t= initial shrimp temperature – shrimp temperature reaches freezing point (°C)</p><p><inline-formula><tex-math id="math-11"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { L } _ { \mathrm { f } } = \end{document} ]]></tex-math></inline-formula> latent heat of freezing shrimp (kJ/Kg)</p><p>4.Frosting effect on the evaporator</p><disp-formula id="equation-4"><tex-math id="math-12"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \begin{array}{l} \mathrm {Q_ {1} = m\times C_ {p} \times\Delta t} \\ \mathrm {Q_ {2} = m\times L_ {f}} \end{array} \end{document} ]]></tex-math></disp-formula><p>Q= cooling capacity (kJ or kW)</p><p>m= frozen shrimp mass (Kg)</p><p>Cp= specific heat capacity of shrimp before freezing (kJ/Kg)</p><p>∆t= initial shrimp temperature – shrimp temperature reaches freezing point (°C)</p><disp-formula id="equation-5"><tex-math id="math-13"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm{L} _ {\mathrm{f}} = \text { latent heat of freezing shrimp (kJ / Kg) } \end{document} ]]></tex-math></disp-formula><p>5.Efficiency of the refrigeratoin system (n)</p><disp-formula id="equation-6"><tex-math id="math-14"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm{n} = \left(\frac {\mathrm{COP} _ {\text {actual}}}{\mathrm{COP} _ {\text {carnot}}}\right) \times 1 0 0 \end{document} ]]></tex-math></disp-formula><p>This eficiency is expressed as a percentage and calculated as the ratio between the actual coeficient of performance (COP) of the system and the Carnot COP, which represents the “theoretical” value derived from the condensation and evaporation temperatures (<xref ref-type="bibr" rid="BIBR-51">Srithar et al., 2025</xref>). The percentages of <inline-formula><tex-math id="math-15"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { C O P } _ { \mathrm { C a r n o t } } \end{document} ]]></tex-math></inline-formula> eficiency levels are presented in <xref ref-type="table" rid="table-4">Table 4</xref>.</p><table-wrap id="table-4"><label>Table 4</label><caption><p><inline-formula><tex-math id="math-16"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { C O P } _ { \mathrm { C a r n o t } } \end{document} ]]></tex-math></inline-formula> eficiency level percentage (<xref ref-type="bibr" rid="BIBR-17">Fianti, 2023</xref>)</p></caption><table><colgroup><col></col><col></col></colgroup><thead><tr><th scope="col">Efficiency level</th><th scope="col">Types of efficiency</th></tr></thead><tbody><tr><td>&gt;100%</td><td>Very Efficient</td></tr><tr><td>76 - 100%</td><td>Efficient</td></tr><tr><td>51 - 75%</td><td>Less Efficient</td></tr><tr><td>26 - 50%</td><td>Not efficient</td></tr><tr><td>1 - 25%</td><td>Very Inefficient</td></tr></tbody></table></table-wrap></sec><sec id="sec-4"><title>Shrimp Test Method</title><p>Shrimp samples were evaluated during the first 20 h of storage in an air blast freezer (ABF). All parameters were analyzed in triplicate at each interval. The pH was measured using a calibrated pH meter on homogenized tissue prepared at a 1:9 ratio, and texture (firmness) was assessed using a simple penetrometer applied to standardized muscle sections. Drip loss was determined gravimetrically by calculating the diference in the sample weight before and after controlled storage. Melanosis was visually evaluated using a simplified scoring scale. The water holding capacity (WHC) was quantified using a centrifugation-based method to determine the percentage of retained moisture. Ice crystal size was observed in thin frozen sections using microscopy. Total volatile base nitrogen (TVB-N) was measured using the Conway difusion method, followed by alkaline titration (<xref ref-type="bibr" rid="BIBR-28">Kim et al., 2020</xref>).</p></sec><sec id="sec-5"><title>Data Analysis</title><p>All thermodynamic performance and shrimp quality parameters were analyzed descriptively and statistically to evaluate the temporal changes during the transient air-blast freezing. The thermodynamic parameters included airflow velocity, air-side temperature diferential (ΔT), evaporator frosting mass, cooling capacity (Q), and the actual coeficient of performance (COP). The shrimp quality parameters included ice crystal size, water-holding capacity (WHC), drip loss, texture, pH, melanosis, and TVB-N. The data are presented in the Results and Discussion sections as tables and figures according to the characteristics of each variable. Descriptive analysis was used to summarize the direction, pattern, and magnitude of changes, whereas statistical analysis was applied, where appropriate, to assess diferences among freezing intervals and examine associations among measured parameters, particularly those related to frosting accumulation, airflow reduction, cooling capacity changes, COP variation, and shrimp quality responses.</p></sec></sec><sec id="sec-6"><title>RESULTS AND DISCUSSION</title><sec id="sec-7"><title>Transient ABF Thermodynamic Behavior</title><p>Transient ABF Thermodynamic Behavior testing was carried out with three treatments at each time, as presented in <xref ref-type="table" rid="table-5">Table 5</xref>.</p><table-wrap id="table-5"><label>Table 5</label><caption><p>Transient ABF performance parameters during early operation</p></caption><table><colgroup><col></col><col></col><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col" rowspan="2">Time (h)</th><th scope="col" colspan="5">Average of 3 measurements each time</th></tr><tr><th scope="col">Airflow (m/s)</th><th scope="col"><inline-formula><tex-math id="math-17"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \Delta T_{air} \end{document} ]]></tex-math></inline-formula> (°C)</th><th scope="col">Frosting (kg, coil)</th><th scope="col">Q (kW)</th><th scope="col">COP (-)</th></tr></thead><tbody><tr><td>0.0</td><td>4.38</td><td>6.48</td><td>0.09</td><td>28.99</td><td>3.51</td></tr><tr><td>0.5</td><td>4.31</td><td>5.60</td><td>0.14</td><td>27.85</td><td>3.40</td></tr><tr><td>1.0</td><td>4.25</td><td>5.16</td><td>0.20</td><td>27.01</td><td>3.21</td></tr><tr><td>1.5</td><td>3.80</td><td>4.60</td><td>0.25</td><td>26.7</td><td>3.15</td></tr><tr><td>2.0</td><td>3.40</td><td>4.49</td><td>0.32</td><td>25.53</td><td>2.94</td></tr><tr><td>2.5</td><td>3.19</td><td>4.32</td><td>0.57</td><td>24.43</td><td>2.78</td></tr><tr><td>3.0</td><td>3.09</td><td>4.19</td><td>0.84</td><td>23.95</td><td>2.71</td></tr><tr><td>3.5</td><td>2.91</td><td>4.05</td><td>1.12</td><td>22.8</td><td>2.56</td></tr><tr><td>4.0</td><td>2.64</td><td>3.86</td><td>1.36</td><td>21.06</td><td>2.37</td></tr><tr><td>4.5</td><td>2.63</td><td>3.85</td><td>1.45</td><td>21</td><td>2.34</td></tr><tr><td>5.0</td><td>2.62</td><td>3.83</td><td>1.50</td><td>20.98</td><td>2.33</td></tr><tr><td>5.5</td><td>2.62</td><td>3.82</td><td>1.49</td><td>20.97</td><td>2.33</td></tr><tr><td>6.0</td><td>2.62</td><td>3.82</td><td>1.49</td><td>29.97</td><td>2.33</td></tr></tbody></table></table-wrap><p><xref ref-type="table" rid="table-5">Table 5</xref> demonstrates a clear transient degradation of the ABF thermodynamic performance during the first 5 h of operation, characterized by a progressive decline in airflow <inline-formula><tex-math id="math-18"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( 4 . 3 8 ~ \to ~ 2 . 6 2 ~ \mathrm { ~ m ~ } ~ \mathsf { s } ^ { - 1 } ) , ~ \Delta \mathrm { T } _ { _ { \mathrm { a i r } } } ~ ( 6 . 4 8 ~ \to ~ \end{document} ]]></tex-math></inline-formula><inline-formula><tex-math id="math-19"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle 3 . 8 3 ~ ^ { \circ } \mathrm { C } ) \end{document} ]]></tex-math></inline-formula> , cooling capacity Q <inline-formula><tex-math id="math-20"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( 2 8 . 9 9 2 0 . 9 8 \end{document} ]]></tex-math></inline-formula> kW), and COP <inline-formula><tex-math id="math-21"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( 3 . 5 1 \ \ 2 . 3 3 ) \end{document} ]]></tex-math></inline-formula>, concomitant with exponential frosting accumulation on the evaporator coil <inline-formula><tex-math id="math-22"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( 0 . 0 9 \mathrm { \div } 1 . 5 0 ~ \mathrm { k g } ) \end{document} ]]></tex-math></inline-formula> . The monotonic reduction in airflow indicates increasing aerodynamic resistance across the coil, which suppresses convective heat transfer and lowers the efective temperature gradient, thereby directly reducing the evaporator heat absorption and system energy eficiency (<xref ref-type="bibr" rid="BIBR-8">Boeng &amp; Stahelin et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-12">de Sa Sarmiento et al., 2025</xref>). This coupled behavior confirms that early stage frost growth acts as a dominant transient thermal resistance layer, impairing both sensible and latent heat exchanges and accelerating COP deterioration (<xref ref-type="bibr" rid="BIBR-23">Jia et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-32">Kumar et al., 2024</xref>).</p><p>The nearly linear decline in Q and COP relative to the frosting mass suggests a strong thermodynamic sensitivity of the system performance to surface blockage during the pre-steady freezing phase. These trends are consistent with recent refrigeration system analyses reporting that frost layer thickening reduces air-side heat transfer coeficients and increases pressure drop, ultimately decreasing system capacity by 15–35% within short operating cycles (<xref ref-type="bibr" rid="BIBR-21">Hermes et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-74">P. Zheng et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-39">C. Ma et al., 2025</xref>). Furthermore, studies on air-blast and cold-room evaporators have confirmed that early transient frosting critically determines downstream product freezing kinetics owing to reduced convective intensity and altered thermal uniformity (<xref ref-type="bibr" rid="BIBR-57">C. Wang et al., 2022</xref>; <xref ref-type="bibr" rid="BIBR-37">S. Liu, Zhang, Li, et al., 2024</xref>). Therefore, the dataset robustly supports the interpretation that transient frosting accumulation is the primary mechanistic driver of early ABF performance decay, with direct implications for freezing rate stability and energy eficiency optimization in exportgrade shrimp-processing systems (<xref ref-type="bibr" rid="BIBR-9">Cezar et al., 2020</xref>; <xref ref-type="bibr" rid="BIBR-67">Yu et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-66">Ye et al., 2024</xref>).</p><table-wrap id="table-6"><label>Table 6</label><caption><p>Pearson correlation matrix (r) calculation (n =11)</p></caption><table><colgroup><col></col><col></col><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col">Variable</th><th scope="col">Airflow</th><th scope="col">ΔT</th><th scope="col">Frosting</th><th scope="col">Q</th><th scope="col">COP</th></tr></thead><tbody><tr><td>Airflow</td><td>1.000</td><td>0.992</td><td>-0.983</td><td>0.994</td><td>0.996</td></tr><tr><td>ΔT</td><td>0.992</td><td>1.000</td><td>-0.975</td><td>0.989</td><td>0.991</td></tr><tr><td>Frosting</td><td>-0.983</td><td>-0.975</td><td>1.000</td><td>-0.987</td><td>-0.989</td></tr><tr><td>Q</td><td>0.994</td><td>0.989</td><td>-0.987</td><td>1.000</td><td>0.998</td></tr><tr><td>COP</td><td>0.996</td><td>0.991</td><td>-0.989</td><td>0.998</td><td>1.000</td></tr></tbody></table></table-wrap><table-wrap id="table-7"><label>Table 7</label><caption><p>Linear regression models of early-stage ABF performance</p></caption><table><colgroup><col></col><col></col><col></col><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col">Dependent variable</th><th scope="col">Regression equation</th><th scope="col">R</th><th scope="col"><inline-formula><tex-math id="math-23"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle R^2 \end{document} ]]></tex-math></inline-formula></th><th scope="col">Adjusted <inline-formula><tex-math id="math-24"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle R^2 \end{document} ]]></tex-math></inline-formula></th><th scope="col">p-value</th><th scope="col">Interpretation</th></tr></thead><tbody><tr><td>COP (-)</td><td>3.64 – 0.86 (Frosting)</td><td>0.989</td><td>0.978</td><td>0.975</td><td>&lt;0.001</td><td>97.8% of COP</td></tr><tr><td>Q (kW)</td><td>29.42 – 5.68</td><td>0.987</td><td>0.973</td><td>0.970</td><td>&lt;0.001</td><td>Cooling</td></tr><tr><td>Airflow (m/s)</td><td>4.47 – 1.25 (Frosting)  (Frosting)</td><td>0.983</td><td>0.966</td><td>0.962</td><td>&lt;0.001</td><td>Frost formation directly restricts airflowvariance explained by frost accumulationcapacity strongly suppressed by frost growth</td></tr></tbody></table></table-wrap><p>Pearson correlation analysis, justified by Shapiro-Wilk normality testing <inline-formula><tex-math id="math-25"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( \mathtt { p } > 0 . 0 5 \end{document} ]]></tex-math></inline-formula> for all variables), revealed an exceptionally strong thermodynamic coupling among the frosting mass, airflow, ΔT, evaporator cooling capacity (Q), and COP during the first 5 h of ABF operation. Frosting exhibited a near-perfect negative association with COP <inline-formula><tex-math id="math-26"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \operatorname { \ 1 r } = - 0 . 9 8 9 \end{document} ]]></tex-math></inline-formula> 9, p &lt; 0.001) and airflow <inline-formula><tex-math id="math-27"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( \mathrm { r } = - 0 . 9 8 3 , \mathrm { p } < 0 . 0 0 1 ) \end{document} ]]></tex-math></inline-formula> , whereas airflow was strongly correlated with Q (r = 0.994) and COP (r = 0.996), confirming a tightly synchronized degradation pathway (<xref ref-type="bibr" rid="BIBR-4">Alarcón-Gallén et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-24">Jiao et al., 2024</xref>). Linear regression further demonstrated that COP decline can be robustly predicted from frosting accumulation according to COP = 3.64 − 0.86(Frosting) with <inline-formula><tex-math id="math-28"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { R } ^ { 2 } = 0 . { \dot { 9 } } 7 8 \end{document} ]]></tex-math></inline-formula> , indicating that nearly 98% of COP variance during early operation is explained by frost growth. Similarly, <inline-formula><tex-math id="math-29"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle \mathrm { ~ Q ~ = ~ 2 9 . 4 2 ~ - ~ 5 . 6 8 ( F r o s t i n g ) } \end{document} ]]></tex-math></inline-formula><inline-formula><tex-math id="math-30"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( \mathrm { R } ^ { 2 } \ : = \ : \end{document} ]]></tex-math></inline-formula> 0.973), substantiating that airflow obstruction induced by frost formation directly suppresses cooling capacity before steady-state conditions are reached (<xref ref-type="bibr" rid="BIBR-30">Klingebiel et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-32">Kumar et al., 2024</xref>).</p><p>These findings move beyond descriptive transient reporting by quantitatively resolving the mechanistic cascade responsible for the early stage performance decay. The process begins with frost deposition on the evaporator surface, which progressively restricts the airflow within the freezing chamber. This airflow restriction reduces the efective heat transfer gradient between the cooling air and the product, leading to the suppression of the cooling capacity of the system. The decline in cooling capacity subsequently results in a measurable degradation of the coeficient of performance (COP).</p><p>The results demonstrate that eficiency loss in industrial Air Blast Freezer (ABF) systems is not merely a time-dependent phenomenon but a statistically predictable process governed by the underlying mechanistic interactions occurring during the early stages of operation (<xref ref-type="bibr" rid="BIBR-58">Wang et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-61">Wu et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-42">Munk et al., 2026</xref>). The near-deterministic correlations observed in this study highlight a critical and previously under-quantified early operation vulnerability window, ofering a predictive framework that can be integrated with product quality kinetics to bridge machine performance dynamics and shrimp microstructural degradation (<xref ref-type="bibr" rid="BIBR-16">Food and Drug Administration, 2022</xref>; <xref ref-type="bibr" rid="BIBR-63">Xu et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-69">Zhang et al., 2025</xref>).</p></sec><sec id="sec-8"><title>Time-Resolved Shrimp Quality Changes</title><p>The changes in shrimp quality attributes during the first 6 h of ABF operation were evaluated to describe the early stage deterioration pattern associated with freezing performance (<xref ref-type="table" rid="table-8">Table 8</xref>).</p><table-wrap id="table-8"><label>Table 8</label><caption><p>Mean Quality dynamics of frozen shrimp during first 6 h ABF operation</p></caption><table><colgroup><col></col><col></col><col></col><col></col><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col">Time (h)</th><th scope="col">Meat pH</th><th scope="col">Texture (N)</th><th scope="col">Drip loss (%)</th><th scope="col">Melanosis (score)</th><th scope="col">WHC (%)</th><th scope="col">Ice crystal (μm)</th><th scope="col">TVB-N (mg N/100g)</th></tr></thead><tbody><tr><td>0.0</td><td>6.95</td><td>11.0</td><td>1.80</td><td>0.9</td><td>86.0</td><td>8.0</td><td>14.0</td></tr><tr><td>0.5</td><td>6.97</td><td>10.8</td><td>1.90</td><td>1.0</td><td>85.0</td><td>9.0</td><td>14.5</td></tr><tr><td>1.0</td><td>6.99</td><td>10.4</td><td>2.00</td><td>1.1</td><td>83.0</td><td>10.0</td><td>15.0</td></tr><tr><td>2.0</td><td>7.04</td><td>9.9</td><td>2.20</td><td>1.2</td><td>81.0</td><td>11.0</td><td>16.0</td></tr><tr><td>3.0</td><td>7.07</td><td>9.4</td><td>2.30</td><td>1.3</td><td>79.0</td><td>13.0</td><td>17.0</td></tr><tr><td>4.0</td><td>7.10</td><td>9.0</td><td>2.40</td><td>1.4</td><td>78.0</td><td>14.0</td><td>18.0</td></tr><tr><td>5.0</td><td>7.11</td><td>8.8</td><td>2.50</td><td>1.5</td><td>77.0</td><td>15.0</td><td>18.0</td></tr><tr><td>6.0</td><td>7.11</td><td>8.7</td><td>2.52</td><td>1.5</td><td>76.8</td><td>15.2</td><td>18.2</td></tr></tbody></table></table-wrap><p>The time-resolved quality profile presented in <xref ref-type="table" rid="table-8">Table 8</xref> demonstrates a clear dynamic response of shrimp muscle properties during the first 6 h of ABF operation, characterized by an early rapid transition phase, followed by a progressive attenuation of change. At the onset (0-1 h), quality parameters exhibited moderate but consistent shifts, with ice crystal size increasing from 8 to 10 µm and WHC declining from 86% to 83%, accompanied by a slight rise in drip loss (1.80-2.00%) and a gradual reduction in texture firmness (11.0-10.4 N). This initial phase reflects the structural adjustment of muscle tissue during primary ice nucleation and crystal growth (<xref ref-type="bibr" rid="BIBR-70">Zhang et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-68">Zhang et al., 2020</xref>; <xref ref-type="bibr" rid="BIBR-1">Ahmad et al., 2025</xref>). Between 2-4 h, the rate of deterioration became more pronounced: ice crystals enlarged from 11 to 14 µm, WHC decreased further to 78%, and firmness dropped to 9.0 N, while drip loss increased to 2.40%. This period indicates intensified intracellular damage, likely associated with reduced freezing eficiency and increased thermal resistance within the system (<xref ref-type="bibr" rid="BIBR-37">Liu et al., 2024</xref>).</p><p>Notably, the melanosis score rose progressively (0.9-1.4), suggesting that oxidative and enzymatic reactions continued despite subzero conditions (Han &amp; Gokoglu, 2022;(<xref ref-type="bibr" rid="BIBR-29">Kittiphattanabawon et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-15">Durage et al., 2025</xref>). After 4 h, the system entered a quasi-stagnation phase, where changes became marginal; the ice crystal size increased only slightly (15.0-15.2 µm), WHC decline slowed (77-76.8%), and drip loss plateaued (2.50- 2.52%). The stabilization of pH (7.11) and the minimal increment in TVB-N (18-18.2 mg N/100 g) further indicate that early structural degradation predominates over biochemical spoilage within this time window (<xref ref-type="bibr" rid="BIBR-52">Sun et al., 2023a</xref>; <xref ref-type="bibr" rid="BIBR-2">Alam et al., 2023c</xref>). Overall, the data reveal a distinct critical period within the first 2–4 h, in which ABF performance exerts the strongest influence on microstructural integrity, while beyond 5 h, the deterioration trend approaches a steady-state condition (<xref ref-type="bibr" rid="BIBR-22">Ji et al., 2021</xref>), highlighting the importance of controlling transient freezing eficiency during the early operational stage to preserve export-grade shrimp quality (<xref ref-type="bibr" rid="BIBR-16">Food and Drug Administration, 2022</xref>; <xref ref-type="bibr" rid="BIBR-59">Wei et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-64">Xu et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-75">Zheng et al., 2026</xref>).</p><p><xref ref-type="table" rid="table-9">Table 9</xref> demonstrates a robust and sequential thermodynamic-microstructuralfunctional linkage during the first 0–6 h of ABF operation, confirming that system performance deterioration propagates mechanistically toward product quality loss. The regression results indicate that COP exerts a strong and significant negative influence on ice crystal size <inline-formula><tex-math id="math-31"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( \beta = 4 . 9 4 ; \mathrm { R } ^ { 2 } = \end{document} ]]></tex-math></inline-formula> 0.97; p &lt; 0.001), indicating that declining refrigeration eficiency directly promotes larger ice crystal formation (<xref ref-type="bibr" rid="BIBR-41">Minh, 2023</xref>). In turn, ice crystal size significantly reduced water-holding capacity (β = -1.17; R² = 0.96; p &lt; 0.001), reflecting the structural disruption of muscle fibers and increased extracellular ice growth. Subsequently, WHC showed a strong inverse relationship with drip loss (β <inline-formula><tex-math id="math-32"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle = - 0 . 0 4 7 ; \mathrm { ~ R } ^ { 2 } = 0 . 9 8 ; \mathrm { ~ p ~ < ~ 0 . 0 0 1 ) } \end{document} ]]></tex-math></inline-formula> , confirming that reduced structural integrity translates into higher exudate release upon thawing (<xref ref-type="bibr" rid="BIBR-52">Sun et al., 2023a</xref>, <xref ref-type="bibr" rid="BIBR-53">2023b</xref>). The total indirect pathway (COP → Ice Crystal → WHC → Drip Loss) exhibited high explanatory power <inline-formula><tex-math id="math-33"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle ( \mathrm { R } ^ { 2 } = \end{document} ]]></tex-math></inline-formula><inline-formula><tex-math id="math-34"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle 0 . 9 4 ; \mathrm { p } < 0 . 0 0 1 ) \end{document} ]]></tex-math></inline-formula> , substantiating that COP does not merely represent an operational eficiency indicator but functions as a predictive upstream determinant of shrimp quality degradation through structural mediation (<xref ref-type="bibr" rid="BIBR-31">Klunklin et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-75">X. Zheng et al., 2026</xref>). Collectively, these findings provide quantitative evidence of a cascading cause-efect mechanism, positioning COP as an early thermodynamic control variable that governs microstructural stability and final functional quality during transient ABF performance.</p><table-wrap id="table-9"><label>Table 9</label><caption><p>Sequential linear regression model of thermodynamic-microstructural-functional quality relationship during 0-6 h ABF operation</p></caption><table><colgroup><col></col><col></col><col></col><col></col><col></col><col></col></colgroup><thead><tr><th scope="col">Regression pathway</th><th scope="col">Regression equation</th><th scope="col">β (slope)</th><th scope="col">R2</th><th scope="col">p-value</th><th scope="col">Interpretation</th></tr></thead><tbody><tr><td>COP → Ice crystal size (μm)</td><td>Ice crystal = 25.62 - 4.94(COP)</td><td>-4.94</td><td>0.97</td><td>&lt;0.001</td><td>Decreasing COP significantly enlarges ice crystals</td></tr><tr><td>Ice crystal size → WHC (%)</td><td>WHC = 94.52 - 1.17(Ice crystal)</td><td>-1.17</td><td>0.96</td><td>&lt;0.001</td><td>Larger crystals significantly reduce water-holding capacity</td></tr><tr><td>WHC → drip loss (%)</td><td>Drip loss = 6.42 - 0.047(WHC)</td><td>-0.047</td><td>0.98</td><td>&lt;0.001</td><td>Lower WHC strongly increases drip loss</td></tr><tr><td>Total indirect effect (COP → drip loss)</td><td>Drip loss ≈ f(COP) via mediators</td><td>—</td><td>0.94</td><td>&lt;0.001</td><td>COP indirectly controls drip loss through structural damage</td></tr></tbody></table></table-wrap></sec><sec id="sec-9"><title>Coupled Machine-Product Interaction</title><p>The transient behavior of the ABF operation was analyzed in relation to ice crystal development to illustrate how changes in freezing performance influence the microstructural formation in shrimp products (<xref ref-type="fig" rid="figure-1">Figure 1</xref>).<xref ref-type="fig" rid="figure-1">Figure 1</xref> illustrates the inverse dynamic relationship between the actual coeficient of performance (COP) of the Air Blast Freezer (ABF) and the evolution of ice crystal size during the first six hours of freezing. At the initial stage (0-1 h), the COP remains relatively high (3.5-3.2), corresponding to smaller ice crystal dimensions (8-10 µm), indicating eficient heat extraction and rapid surface freezing (<xref ref-type="bibr" rid="BIBR-20">Han &amp; Gokoglu, 2022</xref>; <xref ref-type="bibr" rid="BIBR-46">Saini et al., 2021</xref>). As the operation progressed, a gradual decline in COP was observed, reaching approximately 2.3 at 6 h. This thermodynamic deterioration coincided with a steady increase in the ice crystal size to 15 µm. The data suggest that transient eficiency loss, likely associated with frosting accumulation and reduced heat transfer capacity, directly influences freezing kinetics, allowing slower intracellular water solidification and promoting larger crystal formation (<xref ref-type="bibr" rid="BIBR-38">S. Liu, Zhang, Li, et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-45">S et al., 2023</xref>). This pattern confirms that early stage ABF stability plays a decisive role in controlling the microstructural integrity of shrimp muscle during freezing, establishing a mechanistic link between machine performance and product quality (<xref ref-type="bibr" rid="BIBR-56">Tan et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-65">Yan et al., 2023</xref>).<xref ref-type="fig" rid="figure-2">Figure 2</xref> demonstrates a clear divergence between the water holding capacity (WHC) and drip loss throughout the first six hours of freezing. WHC showed a progressive decline from approximately 86% at the initial stage to below 77% at hour six, indicating a gradual impairment of the muscle’s ability to retain intracellular water (<xref ref-type="bibr" rid="BIBR-34">Li et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-27">Kamali et al., 2024</xref>). In parallel, drip loss increased consistently from approximately 1.8% to approximately 2.5%, reflecting intensified exudate release during thawing (<xref ref-type="bibr" rid="BIBR-55">Q. Sun, Zhang, Yang, Hou, et al., 2023</xref>; <xref ref-type="bibr" rid="BIBR-65">Yan et al., 2023</xref>). The near-linear and opposing trajectories of these two parameters indicate a strong inverse association between structural water retention and the physical moisture loss. The transition becomes more pronounced after approximately three hours, suggesting that cumulative microstructural damage, likely associated with enlarging ice crystals, compromises cellular integrity and accelerates extracellular fluid migration (<xref ref-type="bibr" rid="BIBR-76">Zhou et al., 2026</xref>; <xref ref-type="bibr" rid="BIBR-31">Klunklin et al., 2025</xref>). Collectively, the data confirm that transient freezing dynamics critically influence functional quality attributes, with a declining WHC serving as a precursor to measurable drip loss escalation.</p><fig id="figure-1"><label>Figure 1</label><caption><p>Transient ABF versus ice crystal development;</p></caption><long-desc>(   ) = COP; (   ) ice crystal size</long-desc><graphic xlink:href="https://journal.ipb.ac.id/jphpi/article/download/69742/version/50184/34120/417576" mime-subtype="jpeg" mimetype="image"><alt-text>(   ) = COP; (   ) ice crystal size</alt-text></graphic></fig><fig id="figure-2"><label>Figure 2</label><caption><p>Time-resolved changes in WHC and drip loss;</p></caption><long-desc>(   ) = WHC (%),  (   ) = drip loss (%)</long-desc><graphic xlink:href="https://journal.ipb.ac.id/jphpi/article/download/69742/version/50184/34120/417577" mime-subtype="jpeg" mimetype="image"><alt-text>(   ) = WHC (%),  (   ) = drip loss (%)</alt-text></graphic></fig><p><xref ref-type="fig" rid="figure-3">Figure 3</xref> presents the interaction between freezing time and system performance (COP) in terms of drip-loss development. During the high-COP phase (0-3 h), the drip loss increased gradually from approximately 1.8% to 2.3%, indicating controlled moisture migration under relatively stable thermodynamic conditions (<xref ref-type="bibr" rid="BIBR-7">Bao et al., 2023</xref>).</p><fig id="figure-3"><label>Figure 3</label><caption><p>Interaction effect of time and COP on drip loss;</p></caption><long-desc>(   ) = the early observation period, (   ) = the later observation period</long-desc><graphic xlink:href="https://journal.ipb.ac.id/jphpi/article/download/69742/version/50184/34120/417578" mime-subtype="jpeg" mimetype="image"><alt-text>(   ) = the early observation period, (   ) = the later observation period</alt-text></graphic></fig><p>In contrast, once the system transitioned into the lower COP phase (≥3.5 h), the slope of the drip loss became steeper, rising to 2.5% by hour six. This divergence suggests that freezing time alone does not fully explain quality degradation; rather, the combined efects of prolonged exposure and reduced refrigeration eficiency amplify structural damage. This interaction pattern supports the hypothesis that early stage thermodynamic stability moderates moisture retention, whereas declining COP intensifies exudative losses (<xref ref-type="bibr" rid="BIBR-50">Skonieczny et al., 2026</xref>; <xref ref-type="bibr" rid="BIBR-72">Y. Zhao et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-53">K. Sun, Pan, Chen, Tao, et al., 2023</xref>; <xref ref-type="bibr" rid="BIBR-36">L. Liu et al., 2023</xref>; <xref ref-type="bibr" rid="BIBR-43">Phan et al., 2021</xref>). Thus, the time × COP interaction highlights a critical operational window in which maintaining a higher system eficiency can substantially mitigate quality deterioration.<xref ref-type="fig" rid="figure-4">Figure 4</xref> depicts the decomposition of the standardized efects linking COP to the drip loss through a mediation framework. The direct efect of COP on drip loss was negligible and slightly negative (-0.01), indicating that thermodynamic eficiency does not substantially influence moisture loss in the absence of structural intermediaries (<xref ref-type="bibr" rid="BIBR-13">Diao et al., 2021</xref>; <xref ref-type="bibr" rid="BIBR-59">Wei et al., 2024</xref>). In contrast, the indirect efect, quantified at approximately 0.265, dominated the relationship and closely approximated the total efect (0.255). This pattern confirms that the influence of COP on drip loss operates primarily through an intermediate variable, most plausibly ice crystal enlargement, and subsequent microstructural disruption (<xref ref-type="bibr" rid="BIBR-26">Z. Jin et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-73">O. Zheng et al., 2024</xref>). The near equivalence between the indirect and total efects suggests a strong mediation pathway, reinforcing the mechanistic chain whereby declining refrigeration eficiency alters freezing kinetics, modifies crystal morphology, and ultimately increases exudative losses. Collectively, the mediation analysis substantiates that product quality deterioration is not directly driven by energy performance alone, but by its downstream impact on the structural integrity.</p><fig id="figure-4"><label>Figure 4</label><caption><p>Mediation decomposition of COP effect on drip loss</p></caption><graphic xlink:href="https://journal.ipb.ac.id/jphpi/article/download/69742/version/50184/34120/417579" mime-subtype="png" mimetype="image"><alt-text>Figure 4</alt-text></graphic></fig><p><xref ref-type="fig" rid="figure-5">Figure 5</xref> shows the critical transition point in the drip loss development during the first six hours of freezing. Drip loss increased moderately from approximately 1.8% at initiation to approximately 2.3% by the third hour, reflecting relatively controlled structural stress under stable freezing conditions (<xref ref-type="bibr" rid="BIBR-18">Giannakourou &amp; Dermesonlouoglou, 2024</xref>; <xref ref-type="bibr" rid="BIBR-19">Guo et al., 2022</xref>). However, beyond the \~3 h threshold, the trajectory approaches a steeper ascent toward ±2.5%, indicating accelerated exudative release (<xref ref-type="bibr" rid="BIBR-33">LAO et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-60">Wei et al., 2025</xref>). Therefore, the vertical demarcation at hour three therefore represents a pivotal operational window, after which cumulative thermodynamic ineficiencies and microstructural damage become more pronounced (<xref ref-type="bibr" rid="BIBR-65">Yan et al., 2023</xref>; <xref ref-type="bibr" rid="BIBR-76">Zhou et al., 2026</xref>; <xref ref-type="bibr" rid="BIBR-28">Kim et al., 2020</xref>). This inflection suggests that maintaining optimal system performance during the early freezing phase is essential to limit irreversible water migration.</p><p>Consequently, the data support the concept of a “critical freezing window” in which proactive control of heat transfer eficiency can significantly mitigate subsequent quality degradation.</p><p>The most decisive finding of this study is that early stage frost accumulation is the primary upstream driver of both thermodynamic degradation and shrimp microstructural deterioration during transient ABF operation. Frost growth during the first operational hours systematically reduced the airflow, suppressed the air-side temperature gradient, and diminished the cooling capacity and COP with near-deterministic statistical strength. These air-side reductions were synchronously associated with progressive ice crystal enlargement, declining water-holding capacity, and increasing drip loss, confirming that refrigeration eficiency functions as a quality-governing variable rather than merely an energy performance indicator (<xref ref-type="bibr" rid="BIBR-58">Wang Xu et al., 2024</xref>; <xref ref-type="bibr" rid="BIBR-11">da Silva Oliveira &amp; Gonçalves, 2019</xref>; <xref ref-type="bibr" rid="BIBR-49">Sánchez-Vega et al., 2024</xref>).</p><p>Mechanistically, frost deposition increases the thermal resistance and pressure drop across the evaporator, thereby weakening the convective heat transfer intensity (<xref ref-type="bibr" rid="BIBR-74">P. Zheng et al., 2025</xref>). Reduced convective extraction plausibly slows surface heat removal from shrimp tissue, extending the product’s residence time within the critical crystallization temperature zone (approximately -1 to <inline-formula><tex-math id="math-35"><![CDATA[ \documentclass{article} \usepackage{amsmath} \begin{document} \displaystyle { } ^ { - 5 } \ { } ^ { \circ } \mathrm { C } ) \end{document} ]]></tex-math></inline-formula> , where crystal growth kinetics are highly sensitive to the freezing rate. It is important to distinguish direct evidence from thermodynamic inference: airflow, COP, and structural quality parameters were empirically measured, whereas prolonged residence time in the critical zone was inferred from air-side degradation and crystal enlargement patterns (<xref ref-type="bibr" rid="BIBR-4">Alarcón-Gallén et al., 2025</xref>; <xref ref-type="bibr" rid="BIBR-21">Hermes et al., 2021</xref>). Although the product core temperature was not instrumentally monitored, the exceptionally strong inverse regression between the COP and ice crystal size supports the plausibility of this mechanistic pathway.</p><fig id="figure-5"><label>Figure 5</label><caption><p>Identification of the critical freezing window; (   ) = drip loss (%),(-.-.-) = the 3 h reference point</p></caption><graphic xlink:href="https://journal.ipb.ac.id/jphpi/article/download/69742/version/50184/34120/417580" mime-subtype="jpeg" mimetype="image"><alt-text>Figure 5</alt-text></graphic></fig><p>When compared critically with existing refrigeration and frozen seafood studies, the magnitude of the cooling capacity and COP reduction observed in this study aligns with previously reported frost-induced performance losses in industrial evaporators. However, most earlier investigations have treated frosting as an isolated energy eficiency issue or have evaluated shrimp microstructure independently of system thermodynamics. This study advances beyond descriptive alignment by statistically integrating machine performance and product structural response into a sequential mediation framework (COP → Ice Crystal → WHC → Drip Loss), thereby resolving the mechanistic cascade with high explanatory power. This integrative perspective reveals a distinct early operational vulnerability window (approximately 2-4 h), during which thermodynamic instability exerts the strongest influence on crystal morphology before quasi-stable conditions emerge.</p><p>From an operational and HACCP standpoint, airflow decline exceeding approximately one-third of the baseline, COP approaching 3.0, or frost mass nearing 1.0-1.2 kg may serve as practical early warning indicators of accelerated structural degradation. Nevertheless, while the regression pathways exhibit strong predictive capability, the mechanistic interpretation remains confined to measured air-side and structural variables; direct validation of residence time dynamics requires embedded core temperature monitoring and highresolution freezing rate analysis in future investigations.</p></sec></sec><sec id="sec-10"><title>CONCLUSION</title><p>This study demonstrates that early stage performance decay in air-blast freezer operation directly contributes to microstructural and functional quality deterioration in shrimp during the first 6 h of freezing. Frost accumulation reduced airflow, cooling capacity, and COP, whereas the decline in COP was strongly associated with ice crystal enlargement, reduced water-holding capacity, increased drip loss, and texture weakening. 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