{"id":46861,"date":"2019-11-02T01:34:30","date_gmt":"2019-11-02T00:34:30","guid":{"rendered":"https:\/\/www.thermal-engineering.org\/quest-ce-que-lequation-de-continuite-definition\/"},"modified":"2020-03-03T09:00:41","modified_gmt":"2020-03-03T08:00:41","slug":"quest-ce-que-lequation-de-continuite-definition","status":"publish","type":"post","link":"https:\/\/www.thermal-engineering.org\/fr\/quest-ce-que-lequation-de-continuite-definition\/","title":{"rendered":"Qu&#8217;est-ce que l&#8217;\u00e9quation de continuit\u00e9 &#8211; D\u00e9finition"},"content":{"rendered":"<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">L&#8217;\u00e9quation de continuit\u00e9 est simplement une expression math\u00e9matique du principe de conservation de la masse.\u00a0Une \u00e9quation de continuit\u00e9 g\u00e9n\u00e9rale peut \u00e9galement \u00eatre \u00e9crite sous une forme diff\u00e9rentielle.\u00a0G\u00e9nie thermique<\/div>\n<\/div>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2>Conservation de la masse<\/h2>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-quote su-quote-style-default\">\n<div class=\"su-quote-inner su-clearfix\">La masse ne peut \u00eatre ni cr\u00e9\u00e9e ni d\u00e9truite.<\/div>\n<\/div>\n<figure id=\"attachment_14213\" class=\"wp-caption alignright\" aria-describedby=\"caption-attachment-14213\"><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Definition.png\"><img loading=\"lazy\" class=\"size-medium wp-image-14213 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Definition-300x148.png\" alt=\"\u00c9quation de continuit\u00e9 - D\u00e9finition\" width=\"300\" height=\"148\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Definition-300x148.png\" \/><\/a><figcaption id=\"caption-attachment-14213\" class=\"wp-caption-text\">\u00c9quation de continuit\u00e9 &#8211; D\u00e9finition<\/figcaption><\/figure>\n<p>Ce principe est g\u00e9n\u00e9ralement connu sous le nom\u00a0<strong><a title=\"Loi de conservation de la mati\u00e8re\" href=\"https:\/\/www.nuclear-power.com\/laws-of-conservation\/law-of-conservation-of-matter\/\">de principe de conservation de la mati\u00e8re<\/a><\/strong>\u00a0et stipule que la masse d&#8217;un objet ou d&#8217;une collection d&#8217;objets ne change jamais avec le temps, quelle que soit la mani\u00e8re dont les parties constituantes se r\u00e9organisent.\u00a0Ce principe peut \u00eatre utilis\u00e9 dans l&#8217;analyse de\u00a0<strong>fluides en \u00e9coulement<\/strong>\u00a0.\u00a0La conservation de la masse dans\u00a0<a title=\"Dynamique des fluides\" href=\"https:\/\/www.nuclear-power.com\/nuclear-engineering\/fluid-dynamics\/\"><strong>la dynamique des fluides<\/strong><\/a>\u00a0indique que tous\u00a0<strong>les d\u00e9bits massiques dans<\/strong>\u00a0un volume de contr\u00f4le sont \u00e9gaux \u00e0 tous\u00a0<strong>les d\u00e9bits massiques hors<\/strong>\u00a0du volume de contr\u00f4le plus le taux de variation de masse dans le volume de contr\u00f4le.\u00a0Ce principe est exprim\u00e9 math\u00e9matiquement par l&#8217;\u00e9quation suivante:<\/p>\n<p>\u1e41\u00a0<sub>in<\/sub>\u00a0= \u1e41\u00a0<sub>out<\/sub>\u00a0+\u00a0<sup>\u2206m<\/sup>\u00a0\u2044\u00a0<sub>\u2206t<\/sub><\/p>\n<p>Masse entrant par unit\u00e9 de temps = masse quittant par unit\u00e9 de temps + Augmentation de la masse dans le volume de contr\u00f4le par unit\u00e9 de temps<\/p>\n<figure id=\"attachment_14206\" class=\"wp-caption alignright\" aria-describedby=\"caption-attachment-14206\"><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min.png\"><img loading=\"lazy\" class=\"size-medium wp-image-14206 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min-300x300.png\" alt=\"\u00c9quation de continuit\u00e9 - D\u00e9bits dans le r\u00e9acteur\" width=\"300\" height=\"300\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min-300x300.png\" \/><\/a><figcaption id=\"caption-attachment-14206\" class=\"wp-caption-text\">Exemple de d\u00e9bits dans un r\u00e9acteur.\u00a0C&#8217;est un exemple illustratif, les donn\u00e9es ne repr\u00e9sentent aucune conception de r\u00e9acteur.<\/figcaption><\/figure>\n<p>Cette \u00e9quation d\u00e9crit le\u00a0<strong>flux \u00e0 l&#8217;\u00e9tat non stable<\/strong>\u00a0.\u00a0Un \u00e9coulement \u00e0 l&#8217;\u00e9tat non stationnaire fait r\u00e9f\u00e9rence \u00e0 la situation dans laquelle les propri\u00e9t\u00e9s du fluide en un point quelconque du syst\u00e8me peuvent changer au fil du temps.\u00a0<strong>Un \u00e9coulement stable<\/strong>\u00a0correspond \u00e0 la situation dans laquelle les propri\u00e9t\u00e9s du fluide (\u00a0<strong>temp\u00e9rature, pression et vitesse<\/strong>\u00a0) en un point quelconque du syst\u00e8me\u00a0<strong>ne changent pas avec le temps<\/strong>\u00a0.\u00a0Mais l&#8217;une des propri\u00e9t\u00e9s les plus importantes et constantes dans un syst\u00e8me \u00e0 flux stationnaire est le d\u00e9bit massique du syst\u00e8me.\u00a0Cela signifie qu&#8217;il n&#8217;y a\u00a0<strong>pas d&#8217;accumulation<\/strong>\u00a0de masse au sein d&#8217;un composant du syst\u00e8me.<\/p>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<h2><span>\u00c9quation de continuit\u00e9<\/span><\/h2>\n<p><strong><span>L&#8217;\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0est simplement une expression math\u00e9matique du principe de conservation de la masse.\u00a0Pour un volume de contr\u00f4le qui a une\u00a0<\/span><strong><span>seule entr\u00e9e<\/span><\/strong><span>\u00a0et une\u00a0<\/span><strong><span>seule sortie<\/span><\/strong><span>\u00a0, le principe de conservation de la masse stipule que, pour\u00a0<\/span><strong><span>un d\u00e9bit en r\u00e9gime permanent<\/span><\/strong><span>\u00a0, le d\u00e9bit massique dans le volume doit \u00eatre \u00e9gal au d\u00e9bit massique sortant.<\/span><\/p>\n<p><span>\u1e41\u00a0<\/span><sub><span>in<\/span><\/sub><span>\u00a0= \u1e41\u00a0<\/span><sub><span>out<\/span><\/sub><\/p>\n<p><span>Masse entrant par unit\u00e9 de temps = Masse sortant par unit\u00e9 de temps<\/span><\/p>\n<p><span>Cette \u00e9quation est appel\u00e9e\u00a0<\/span><strong><span>\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0pour un \u00e9coulement unidimensionnel stable.\u00a0Pour un d\u00e9bit constant \u00e0 travers un volume de contr\u00f4le avec de nombreuses entr\u00e9es et sorties, le d\u00e9bit massique net doit \u00eatre nul, o\u00f9 les entr\u00e9es sont n\u00e9gatives et les sorties sont positives.<\/span><\/p>\n<p><span>Ce principe peut \u00eatre appliqu\u00e9 \u00e0 un\u00a0<\/span><strong><span>streamtube<\/span><\/strong><span>\u00a0tel que celui illustr\u00e9 ci-dessus.\u00a0Aucun fluide ne s&#8217;\u00e9coule \u00e0 travers la limite\u00a0cr\u00e9\u00e9e\u00a0par les\u00a0<\/span><strong><span>lignes de courant, de<\/span><\/strong><span>\u00a0sorte que la masse entre et sort uniquement par les deux extr\u00e9mit\u00e9s de cette section de tube de courant.<\/span><\/p>\n<p><span>Lorsqu&#8217;un fluide est en mouvement, il doit se d\u00e9placer de mani\u00e8re \u00e0 conserver la masse.\u00a0Pour voir comment la conservation de la masse impose des restrictions sur le champ de vitesse, consid\u00e9rez l&#8217;\u00e9coulement r\u00e9gulier de fluide \u00e0 travers un conduit (c&#8217;est-\u00e0-dire que les d\u00e9bits d&#8217;entr\u00e9e et de sortie ne varient pas avec le temps).<\/span><\/p>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2><span>Forme diff\u00e9rentielle d&#8217;\u00e9quation de continuit\u00e9<\/span><\/h2>\n<p><span>Une \u00e9quation g\u00e9n\u00e9rale de continuit\u00e9 peut \u00e9galement s&#8217;\u00e9crire sous une\u00a0<\/span><strong><span>forme diff\u00e9rentielle<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><sup><span>\u2202\u2374<\/span><\/sup><span>\u00a0\u2044\u00a0<\/span><sub><span>\u2202t<\/span><\/sub><span>\u00a0+ \u2207.\u00a0(\u2374 \u035ev) = \u03c3<\/span><\/p>\n<p><strong><span>o\u00f9<\/span><\/strong><\/p>\n<ul>\n<li><span>\u2207.\u00a0est la divergence,<\/span><\/li>\n<li><span>\u03c1 est la densit\u00e9 de la quantit\u00e9 q,<\/span><\/li>\n<li><span>\u2374 \u035ev est le flux de quantit\u00e9 q,<\/span><\/li>\n<li><span>\u03c3 est la g\u00e9n\u00e9ration de q par unit\u00e9 de volume par unit\u00e9 de temps.\u00a0Les termes qui g\u00e9n\u00e8rent (\u03c3&gt; 0) ou suppriment (\u03c3 &lt;0) q sont appel\u00e9s respectivement \u00absources\u00bb et \u00abpuits\u00bb.\u00a0Si q est une quantit\u00e9 conserv\u00e9e (telle que l&#8217;\u00e9nergie), \u03c3 est \u00e9gal \u00e0 0.<\/span><\/li>\n<\/ul>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2><span>\u00c9quation de continuit\u00e9 &#8211; plusieurs entr\u00e9es et sorties<\/span><\/h2>\n<p><span>Pour un volume de contr\u00f4le avec\u00a0<\/span><strong><span>plusieurs entr\u00e9es et sorties<\/span><\/strong><span>\u00a0, le principe de conservation de la masse exige que la\u00a0<\/span><strong><span>somme des d\u00e9bits massiques dans<\/span><\/strong><span>\u00a0le volume de contr\u00f4le soit \u00e9gale \u00e0 la\u00a0<\/span><strong><span>somme des d\u00e9bits massiques hors<\/span><\/strong><span>\u00a0du volume de contr\u00f4le.\u00a0<\/span><strong><span>L&#8217;\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0pour cette situation plus g\u00e9n\u00e9rale s&#8217;exprime par l&#8217;\u00e9quation suivante:<\/span><\/p>\n<p><span>\u2211\u1e41\u00a0<\/span><sub><span>in<\/span><\/sub><span>\u00a0= \u2211\u1e41\u00a0<\/span><sub><span>out<\/span><\/sub><\/p>\n<p><span>Somme des d\u00e9bits massiques entrant par unit\u00e9 de temps = Somme des d\u00e9bits massiques sortant par unit\u00e9 de temps<\/span><\/p>\n<div class=\"su-divider su-divider-style-dotted\"><\/div>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<div class=\"su-spacer\"><\/div>\n<h2><span>\u00c9quation de continuit\u00e9 &#8211; Exemples<\/span><\/h2>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\">\n<h2><span>D\u00e9bit \u00e0 travers un c\u0153ur de r\u00e9acteur<\/span><\/h2>\n<p><span>Dans cet exemple, nous calculerons le\u00a0<\/span><strong><span>d\u00e9bit \u00e0<\/span><\/strong><span>\u00a0travers un\u00a0<\/span><a title=\"Noyau du r\u00e9acteur\" href=\"https:\/\/www.reactor-physics.com\/what-is-reactor-core-definition\/\"><span>c\u0153ur<\/span><\/a><span>\u00a0de\u00a0<a title=\"Noyau du r\u00e9acteur\" href=\"https:\/\/www.reactor-physics.com\/what-is-reactor-core-definition\/\">r\u00e9acteur \u00e0<\/a>\u00a0partir de l&#8217;\u00e9quation de continuit\u00e9.\u00a0Il s&#8217;agit d&#8217;un exemple illustratif, les donn\u00e9es suivantes ne repr\u00e9sentent aucune conception de r\u00e9acteur.<\/span><\/p>\n<p><span>\u1e41\u00a0<\/span><sub><span>in<\/span><\/sub><span>\u00a0= \u1e41\u00a0<\/span><sub><span>out<\/span><\/sub><\/p>\n<p><span>(\u03c1Av)\u00a0<\/span><sub><span>in<\/span><\/sub><span>\u00a0= (\u03c1Av)\u00a0<\/span><sub><span>out<\/span><\/sub><\/p>\n<p><span>____________________________<\/span><\/p>\n<figure id=\"attachment_14174\" class=\"wp-caption alignright\" aria-describedby=\"caption-attachment-14174\"><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/water-density-temperature.png\"><img loading=\"lazy\" class=\"size-medium wp-image-14174 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/water-density-temperature-300x211.png\" alt=\"Graphique - densit\u00e9 - eau - temp\u00e9rature\" width=\"300\" height=\"211\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/water-density-temperature-300x211.png\" \/><\/a><figcaption id=\"caption-attachment-14174\" class=\"wp-caption-text\"><span>Densit\u00e9 en fonction de la temp\u00e9rature de l&#8217;eau<\/span><\/figcaption><\/figure>\n<p><a title=\"PWR - R\u00e9acteur \u00e0 eau sous pression\" href=\"https:\/\/www.nuclear-power.com\/pwr-pressurized-water-reactor\/\"><strong><span>Les r\u00e9acteurs \u00e0 eau sous pression<\/span><\/strong><\/a><span>\u00a0sont refroidis et mod\u00e9r\u00e9s par<\/span><strong><span>\u00a0de l&#8217;eau liquide \u00e0 haute pression<\/span><\/strong><span>\u00a0(<\/span><strong><span>\u00a0par exemple 16 MPa<\/span><\/strong><span>\u00a0).\u00a0\u00c0 cette pression, l&#8217;eau bout \u00e0 environ<\/span><strong><span>\u00a0350 \u00b0 C (662 \u00b0 F)<\/span><\/strong><span>\u00a0.\u00a0La temp\u00e9rature d&#8217;entr\u00e9e de l&#8217;eau est d&#8217;environ<\/span><strong><span>\u00a0290 \u00b0 C<\/span><\/strong><span>\u00a0(<\/span><strong><span>\u00a0\u2374 ~ 720 kg \/ m\u00a0<\/span><sup><span>3<\/span><\/sup><\/strong><span>\u00a0).\u00a0L&#8217;eau (liquide de refroidissement) est chauff\u00e9e dans le c\u0153ur du r\u00e9acteur \u00e0 environ<\/span><strong><span>\u00a0325 \u00b0 C<\/span><\/strong><span>\u00a0(<\/span><strong><span>\u00a065 ~ 654 kg \/ m\u00a0<\/span><sup><span>3<\/span><\/sup><\/strong><span>\u00a0) lorsque l&#8217;eau s&#8217;\u00e9coule \u00e0 travers le c\u0153ur.<\/span><br \/>\n<span>Le circuit primaire d&#8217;un<\/span><strong><span>\u00a0PWR<\/span><\/strong><span>\u00a0typique\u00a0est divis\u00e9 en 4 boucles ind\u00e9pendantes (diam\u00e8tre de la tuyauterie ~ 700 mm), chaque boucle comprend un<\/span><strong><a title=\"G\u00e9n\u00e9rateur de vapeur\" href=\"https:\/\/www.nuclear-power.com\/steam-generator\/\"><span>\u00a0g\u00e9n\u00e9rateur de vapeur<\/span><\/a><\/strong><span>\u00a0et une<\/span><strong><a title=\"Pompe de refroidissement du r\u00e9acteur\" href=\"https:\/\/www.nuclear-power.com\/reactor-coolant-pump\/\"><span>\u00a0pompe de refroidissement principale<\/span><\/a><\/strong><span>.\u00a0\u00c0 l&#8217;int\u00e9rieur de la cuve du r\u00e9acteur (RPV), le liquide de refroidissement descend d&#8217;abord \u00e0 l&#8217;ext\u00e9rieur du c\u0153ur du r\u00e9acteur (\u00e0\u00a0<\/span><strong><span>travers le tuyau de descente<\/span><\/strong><span>\u00a0).\u00a0Depuis le fond de l&#8217;enceinte sous pression, le flux est\u00a0<\/span><strong><span>invers\u00e9 vers le haut \u00e0 travers le c\u0153ur<\/span><\/strong><span>\u00a0, o\u00f9 la temp\u00e9rature du liquide de refroidissement augmente lors de son passage \u00e0 travers les crayons de combustible et les assemblages form\u00e9s par eux.<\/span><\/p>\n<h2><span>Calculer:<\/span><\/h2>\n<ul>\n<li><span>le d\u00e9bit volum\u00e9trique de la tuyauterie primaire (m\u00a0<\/span><sup><span>3<\/span><\/sup><span>\u00a0\/ s),<\/span><\/li>\n<li><span>la vitesse d&#8217;\u00e9coulement de la tuyauterie primaire (m \/ s),<\/span><\/li>\n<li><span>la vitesse d&#8217;\u00e9coulement \u00e0 l&#8217;entr\u00e9e du c\u0153ur (m \/ s),<\/span><\/li>\n<li><span>la vitesse d&#8217;\u00e9coulement de sortie du c\u0153ur (m \/ s)<\/span><\/li>\n<\/ul>\n<p><span>quand<\/span><\/p>\n<ul>\n<li><span>le d\u00e9bit massique dans la branche chaude de la tuyauterie primaire est \u00e9gal \u00e0\u00a0<\/span><strong><span>4648 kg \/ s<\/span><\/strong><span>\u00a0,<\/span><\/li>\n<li><span>La section de flux du c\u0153ur du r\u00e9acteur est \u00e9gale \u00e0\u00a0<\/span><strong><span>5 m\u00a0<\/span><sup><span>2<\/span><\/sup><\/strong><span>\u00a0,<\/span><\/li>\n<li><span>La section transversale du d\u00e9bit de la tuyauterie primaire (boucle unique) est \u00e9gale \u00e0\u00a0<\/span><strong><span>0,38 m\u00a0<\/span><sup><span>2<\/span><\/sup><\/strong><\/li>\n<\/ul>\n<h2><span>R\u00e9sultats:<\/span><\/h2>\n<figure id=\"attachment_14206\" class=\"wp-caption alignright\" aria-describedby=\"caption-attachment-14206\"><a href=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min.png\"><img loading=\"lazy\" class=\"wp-image-14206 lazy-loaded\" src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min.png\" alt=\"\u00c9quation de continuit\u00e9 - D\u00e9bits dans le r\u00e9acteur\" width=\"400\" height=\"400\" data-lazy-type=\"image\" data-src=\"https:\/\/thermal-engineering.org\/wp-content\/uploads\/2019\/05\/Continuity-Equation-Flow-Rate-min.png\" \/><\/a><figcaption id=\"caption-attachment-14206\" class=\"wp-caption-text\"><span>Exemple de d\u00e9bits dans un r\u00e9acteur.\u00a0Il s&#8217;agit d&#8217;un exemple illustratif, les donn\u00e9es ne repr\u00e9sentent aucune conception de r\u00e9acteur.<\/span><\/figcaption><\/figure>\n<p><span>D\u00e9bit volum\u00e9trique jambe froide:<\/span><\/p>\n<p><strong><span>Q\u00a0<\/span><sub><span>froid<\/span><\/sub><span>\u00a0\u00a0= \u1e41 \/ \u2374<\/span><\/strong><span>\u00a0= 4648\/720 = 6,46 m\u00a0<\/span><sup><span>3<\/span><\/sup><span>\u00a0\/ s =\u00a0<\/span><strong><span>23240 m\u00a0<\/span><sup><span>3<\/span><\/sup><span>\u00a0\/ hod<\/span><\/strong><\/p>\n<p><span>Vitesse d&#8217;\u00e9coulement des jambes froides:<\/span><\/p>\n<p><span>A\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0\u00a0= \u03c0.d\u00a0<\/span><sup><span>deux<\/span><\/sup><span>\u00a0\/ quatre<\/span><\/p>\n<p><strong><span>v\u00a0<\/span><sub><span>froid<\/span><\/sub><\/strong><span>\u00a0\u00a0=\u00a0<\/span><strong><span>Q\u00a0<\/span><sub><span>froid<\/span><\/sub><\/strong><strong><span>\u00a0\u00a0\/ D\u00a0<\/span><sub><span>1<\/span><\/sub><\/strong><span>\u00a0\u00a0= 6,46 \/ (3,14 x 0,7\u00a0<\/span><sup><span>2<\/span><\/sup><span>\u00a0\/4) = 6,46 \/ 0,38 =\u00a0<\/span><strong><span>17 m \/ s<\/span><\/strong><\/p>\n<p><span>D\u00e9bit volum\u00e9trique de la jambe chaude:<\/span><\/p>\n<p><strong><span>Q\u00a0<\/span><sub><span>chaud<\/span><\/sub><span>\u00a0\u00a0= \u1e41 \/ \u2374<\/span><\/strong><span>\u00a0= 4648\/654 = 7,11 m\u00a0<\/span><sup><span>3<\/span><\/sup><span>\u00a0\/ s =\u00a0<\/span><strong><span>25585 m\u00a0<\/span><sup><span>3<\/span><\/sup><span>\u00a0\/ hod<\/span><\/strong><\/p>\n<p><span>Vitesse d&#8217;\u00e9coulement des jambes chaudes:<\/span><\/p>\n<p><span>A = \u03c0.d\u00a0<\/span><sup><span>deux<\/span><\/sup><span>\u00a0\/ quatre<\/span><\/p>\n<p><strong><span>v\u00a0<\/span><sub><span>chaud<\/span><\/sub><\/strong><span>\u00a0\u00a0=\u00a0<\/span><strong><span>Q\u00a0<\/span><sub><span>chaud<\/span><\/sub><span>\u00a0\u00a0\/ A\u00a0<\/span><sub><span>1<\/span><\/sub><\/strong><span>\u00a0\u00a0= 7,11 \/ (3,14 x 0,7\u00a0<\/span><sup><span>2<\/span><\/sup><span>\u00a0\/4) = 7,11 \/ 0,38 =\u00a0<\/span><strong><span>18,7 m \/ s<\/span><\/strong><\/p>\n<p><span>ou selon\u00a0<\/span><strong><span>l&#8217;\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><strong><span>\u2374\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0.\u00a0A\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>2<\/span><\/sub><span>\u00a0.\u00a0A\u00a0<\/span><sub><span>2<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>2<\/span><\/sub><\/strong><\/p>\n<p><strong><span>v\u00a0<\/span><sub><span>chaud<\/span><\/sub><\/strong><span>\u00a0= v\u00a0<\/span><sub><span>froid<\/span><\/sub><span>\u00a0.\u00a0\u2374\u00a0<\/span><sub><span>froid<\/span><\/sub><span>\u00a0\/ \u2374\u00a0<\/span><sub><span>chaud<\/span><\/sub><span>\u00a0= 17 x 720\/654 =\u00a0<\/span><strong><span>18,7 m \/ s<\/span><\/strong><\/p>\n<p><span>Vitesse d&#8217;\u00e9coulement \u00e0 l&#8217;entr\u00e9e du c\u0153ur:<\/span><\/p>\n<p><span>Un\u00a0<\/span><sub><span>noyau<\/span><\/sub><span>\u00a0= 5m\u00a0<\/span><sup><span>2<\/span><\/sup><\/p>\n<p><span>A\u00a0<\/span><sub><span>tuyauterie<\/span><\/sub><span>\u00a0= 4 x A\u00a0<\/span><sub><span>1<\/span><\/sub><span>\u00a0= 4 x 0,38 = 1,52 m\u00a0<\/span><sup><span>2<\/span><\/sup><\/p>\n<p><span>\u2374\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>froid<\/span><\/sub><\/p>\n<p><span>selon\u00a0<\/span><strong><span>l&#8217;\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><span>\u2374\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0.\u00a0Un\u00a0<\/span><sub><span>noyau<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>froid<\/span><\/sub><span>\u00a0.\u00a0Un\u00a0<\/span><sub><span>passepoil<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>froid<\/span><\/sub><\/p>\n<p><strong><span>v\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><\/strong><span>\u00a0= v\u00a0<\/span><sub><span>froid<\/span><\/sub><span>\u00a0.\u00a0Une\u00a0<\/span><sub><span>tuyauterie<\/span><\/sub><span>\u00a0\/ un\u00a0<\/span><sub><span>noyau<\/span><\/sub><span>\u00a0A\u00a0= 17 x 1,52 \/ 5 =\u00a0<\/span><strong><span>5,17 m \/ s<\/span><\/strong><\/p>\n<p><span>Vitesse d&#8217;\u00e9coulement de sortie du c\u0153ur:<\/span><\/p>\n<p><span>\u2374\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>froid<\/span><\/sub><\/p>\n<p><span>\u2374\u00a0<\/span><sub><span>sortie<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>chaud<\/span><\/sub><\/p>\n<p><span>selon\u00a0<\/span><strong><span>l&#8217;\u00e9quation de continuit\u00e9<\/span><\/strong><span>\u00a0:<\/span><\/p>\n<p><span>\u2374\u00a0<\/span><sub><span>sortie<\/span><\/sub><span>\u00a0.\u00a0Un\u00a0<\/span><sub><span>noyau<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>sortie<\/span><\/sub><span>\u00a0= \u2374\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0.\u00a0Un\u00a0<\/span><sub><span>noyau<\/span><\/sub><span>\u00a0.\u00a0v\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><br \/>\n<strong><span>v\u00a0<\/span><sub><span>sortie<\/span><\/sub><\/strong><span>\u00a0= v\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0.\u00a0\u2374\u00a0<\/span><sub><span>entr\u00e9e<\/span><\/sub><span>\u00a0\/ \u2374\u00a0<\/span><sub><span>sortie<\/span><\/sub><span>\u00a0= 5,17 x 720\/654 =\u00a0<\/span><strong><span>5,69 m \/ s<\/span><\/strong><\/p>\n<\/div>\n<\/div>\n<div class=\"lgc-column lgc-grid-parent lgc-grid-100 lgc-tablet-grid-100 lgc-mobile-grid-100 lgc-equal-heights  lgc-first lgc-last\">\n<div class=\"inside-grid-column\"><\/div>\n<\/div>\n<\/div>\n<\/div>\n<p>&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;&#8230;.<\/p>\n<p>Cet article est bas\u00e9 sur la traduction automatique de l&#8217;article original en anglais. Pour plus d&#8217;informations, voir l&#8217;article en anglais. Pouvez vous nous aider Si vous souhaitez corriger la traduction, envoyez-la \u00e0 l&#8217;adresse: translations@nuclear-power.com ou remplissez le formulaire de traduction en ligne. Nous appr\u00e9cions votre aide, nous mettrons \u00e0 jour la traduction le plus rapidement possible. Merci<\/p>\n","protected":false},"excerpt":{"rendered":"<p>L&#8217;\u00e9quation de continuit\u00e9 est simplement une expression math\u00e9matique du principe de conservation de la masse.\u00a0Une \u00e9quation de continuit\u00e9 g\u00e9n\u00e9rale peut \u00e9galement \u00eatre \u00e9crite sous une forme diff\u00e9rentielle.\u00a0G\u00e9nie thermique Conservation de la masse La masse ne peut \u00eatre ni cr\u00e9\u00e9e ni d\u00e9truite. \u00c9quation de continuit\u00e9 &#8211; D\u00e9finition Ce principe est g\u00e9n\u00e9ralement connu sous le nom\u00a0de principe &#8230; <a title=\"Qu&#8217;est-ce que l&#8217;\u00e9quation de continuit\u00e9 &#8211; D\u00e9finition\" class=\"read-more\" href=\"https:\/\/www.thermal-engineering.org\/fr\/quest-ce-que-lequation-de-continuite-definition\/\" aria-label=\"En savoir plus sur Qu&#8217;est-ce que l&#8217;\u00e9quation de continuit\u00e9 &#8211; D\u00e9finition\">Lire la suite<\/a><\/p>\n","protected":false},"author":1,"featured_media":0,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":[],"categories":[8],"tags":[],"yoast_head":"<!-- This site is optimized with the Yoast SEO plugin v15.4 - https:\/\/yoast.com\/wordpress\/plugins\/seo\/ -->\n<title>Qu&#039;est-ce que l&#039;\u00e9quation de continuit\u00e9 - D\u00e9finition<\/title>\n<meta name=\"description\" content=\"L&#039;\u00e9quation de continuit\u00e9 est simplement une expression math\u00e9matique du principe de conservation de la masse. 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