Posts filled under #ilovemybody

 Son Bir Yl  Bu  fotoraf

Son Bir Yl Bu fotoraf son bir ylmdan. * Soldan ilk fotoraf, Eyll 2015te doum yaptktan 9 ay sonra, Mays 2016da bir etkinlikte ekildi. Bu 9 aylk dnemde haftada 3 gn spor yapmama ramen 66 kg civarndaydm. Spor salonunda ise antrenmanlarm rutin, aletli ve arlk temelli ilerliyordu. Sporda performansm ykselmiyordu ve isteksizdim. Artk temel bir eylerin yetersizliinden emindim. Beslenme ve gda konusunda daha yaln modelleri aramaya baladm. Ancak bunu yaparken kesinlikle psikolojimi ve sosyal yaamm etkileyecek diyetleri uygulamak istemediimi iyi biliyordum. * Ortadaki fotorafm ise Haziran 2017de ekildi. ubat 2017de intolerans testi yaptrdm. Test sonucu bana dokunan gdalarn buday, karabiber, kuzu eti ve ilek olduunu rendim. Benim bnyeme negatif etkisi olan (asitik etki, mide yanmas, cilt sorunlar, ikinlik vb.) bu gdalar 4 ay boyunca tamamen braktm. Ek olarak bu 4 ay boyunca nceden olduka azalttm endstriyel ekeri de braktm. Spor programm da tamamen deitirdim ve beden arl ile yaplan Calisthenics antrenmanlarna baladm. Sonu 4 ayda 61 kilo ve daha enerjik, salkl bir beden ve zihin. * En sadaki fotorafm 20 Austos 2017de ekildi. ki ay gibi ksa bir srede 56 kiloya zellikle kas ktlemi koruyarak indim. Benim iin bile 56 kiloda daha fazla ya yakm olmak olduka artc bir sonu oldu. Neler yaptm; Calisthenics antrenmanlarna haftada 3 gn devam ettim. Bol salkl ya, bol sebze, dengeli protein ile gnde 2 n beslenmeye adm adm gei yaptm. zellikle endstriyel eker ve buday ieren rnleri tketmedim. Gei dneminde zorlandm anlarda meyveler ie yarad. * Vcudumun birincil enerji kayna olarak ya kulland bu yeni dnemde gda tercihlerim sayesinde, vcudumun negatif tepkileri de ciddi dzeyde azald. Trnak, cilt, mide, barsak skntlarm hi ila kullanmadan belirgin ekilde azald. Enerjim uzun sreli ve gn boyunca yksek ve keyfim ise yerinde. Voila!!! #health #fitness #calisthenics #cleanmind #cleanbody #cleanfood #intermittentfasting #nosugar #fitmama #foodporn #abs #ilovemybody #iyilikherzamankazanr

Sai cosa bevo?
 Restorate

Sai cosa bevo? Restorate sali minerali.... sai a cosa servono ???? A me ha aiutato per il reflusso gastrico, per i crampi notturni e a rinforzare capelli e unghie ...... io lo adoro, in pi mi fa fare delle dormitone .... assolutamente da provare. #sport #movimento #pminternational #solointegrazione #ilovemybody ##body #benessere #fitline #irenestrongtraining #depurarsi #fitnessfashion #benessere #benesserefisico #rimettersiinforma #sport #sportgirl #trainingday #motivazione #obiettivi #networker #corpo #fitnessmodel #fitmamma #fitnessmamma #allenamento #tatoomodel #restorate

"My beloved child, break

"My beloved child, break your heart no longer. Each time you judge yourself you break your own heart" - Bapuji | I've been dealing with negative self talk for years like most people, lately however I've started to find a peaceful balance with my health and body image issues. We do have so much power to be positive and kind towards ourselves, and it's so important to be vigilant in our everyday practice of self love. I've started taking care of myself physically by eating better and slowly but surely starting a exercise routine that works for me. I've lost 10lbs and feel better and better everyday! #selflove #mindfulliving #consciousnessshift #wildatheart #powerofnow #joyboy #gayman #gayblogger #nobodyshaming #ilovemybody #guys #gaypic # #queermen #positivevibes #healthylivingjourney #gayspirit #gaysoul #guywithtattoos #yoga #running #excercise #selfcaresunday #selfcare #gaymen #gaygeek #spirituality #practice #onedayatatime

Nein, wir machen keine Di

Nein, wir machen keine Dit! Nein, wir haben kein Jo-Jo-Problem! Nein, wir hungern nicht! Gesunde Ernhrung bedeutet, seinem Krper den ntigen #Respekt zu erweisen! Sich gesund zu ernhren und zu oder abzunehmen ist viel leichter als man denkt. Wichtig ist, dass der Krper mit allem versorgt wird, was er braucht. Dazu zhlen rund 50 Nhrstoffe in ausreichender Menge, darunter Kohlenhydrate, Fett und Eiwei, sowie Vitamine, Mineralstoffe und Spurenelemente. Gesunde Ernhrung bedeutet nicht, dass man lebenslang komplett auf alle Leckereien, se Snden, genuvolle Momente usw. verzichten muss! Die richtige Mischung und auch die Menge macht's! Je nach dem, was man fr ein Ziel anstrebt, 1 bis 2 mal tglich unser #Powerfood 2 - 3 Liter Wasser am Tag Dazu unser tgliches 10-Minuten-Workout bequem von Zuhause aus, oder wo auch immer du willst Das ist schon das ganze Geheimnis #Verbotesindverboten Keine Punkte oder Kalorien zhlen! Kein Hungern! OSC ist unkompliziert, preisWert, effektiv und gesund! Was will man mehr? #healthy #healthyfood #powerfood #ilovemylife #lebenslust #ilovemybody #leben #lebensfreude #enjoylife #sun #havefun #dit #geheimnis

Don't you think it's amaz

Don't you think it's amazing? What our bodys can do! On the first picture my weight was almost 80kg i was very sick and couldn't loose weight vs. 58kg on the right one. I've been blessed with no stretch marks, and i think thats amazing because of that body different i love my body, it helps me all day long! Thank you #ilovemybody #mybody

An extract on #ilovemybody

Large scale industrial distillation applications include both batch and continuous fractional, vacuum, azeotropic, extractive, and steam distillation. The most widely used industrial applications of continuous, steady-state fractional distillation are in petroleum refineries, petrochemical and chemical plants and natural gas processing plants. To control and optimize such industrial distillation, a standardized laboratory method, ASTM D86, is established. This test method extends to the atmospheric distillation of petroleum products using a laboratory batch distillation unit to quantitatively determine the boiling range characteristics of petroleum products. Industrial distillation is typically performed in large, vertical cylindrical columns known as distillation towers or distillation columns with diameters ranging from about 65 centimeters to 16 meters and heights ranging from about 6 meters to 90 meters or more. When the process feed has a diverse composition, as in distilling crude oil, liquid outlets at intervals up the column allow for the withdrawal of different fractions or products having different boiling points or boiling ranges. The "lightest" products (those with the lowest boiling point) exit from the top of the columns and the "heaviest" products (those with the highest boiling point) exit from the bottom of the column and are often called the bottoms. Industrial towers use reflux to achieve a more complete separation of products. Reflux refers to the portion of the condensed overhead liquid product from a distillation or fractionation tower that is returned to the upper part of the tower as shown in the schematic diagram of a typical, large-scale industrial distillation tower. Inside the tower, the downflowing reflux liquid provides cooling and condensation of the upflowing vapors thereby increasing the efficiency of the distillation tower. The more reflux that is provided for a given number of theoretical plates, the better the tower's separation of lower boiling materials from higher boiling materials. Alternatively, the more reflux that is provided for a given desired separation, the fewer the number of theoretical plates required. Chemical engineers must choose what combination of reflux rate and number of plates is both economically and physically feasible for the products purified in the distillation column. Such industrial fractionating towers are also used in cryogenic air separation, producing liquid oxygen, liquid nitrogen, and high purity argon. Distillation of chlorosilanes also enables the production of high-purity silicon for use as a semiconductor. Design and operation of a distillation tower depends on the feed and desired products. Given a simple, binary component feed, analytical methods such as the McCabeThiele method or the Fenske equation can be used. For a multi-component feed, simulation models are used both for design and operation. Moreover, the efficiencies of the vaporliquid contact devices (referred to as "plates" or "trays") used in distillation towers are typically lower than that of a theoretical 100% efficient equilibrium stage. Hence, a distillation tower needs more trays than the number of theoretical vaporliquid equilibrium stages. A variety of models have been postulated to estimate tray efficiencies. In modern industrial uses, a packing material is used in the column instead of trays when low pressure drops across the column are required. Other factors that favor packing are: vacuum systems, smaller diameter columns, corrosive systems, systems prone to foaming, systems requiring low liquid holdup, and batch distillation. Conversely, factors that favor plate columns are: presence of solids in feed, high liquid rates, large column diameters, complex columns, columns with wide feed composition variation, columns with a chemical reaction, absorption columns, columns limited by foundation weight tolerance, low liquid rate, large turn-down ratio and those processes subject to process surges. This packing material can either be random dumped packing (13" wide) such as Raschig rings or structured sheet metal. Liquids tend to wet the surface of the packing and the vapors pass across this wetted surface, where mass transfer takes place. Unlike conventional tray distillation in which every tray represents a separate point of vaporliquid equilibrium, the vaporliquid equilibrium curve in a packed column is continuous. However, when modeling packed columns, it is useful to compute a number of "theoretical stages" to denote the separation efficiency of the packed column with respect to more traditional trays. Differently shaped packings have different surface areas and void space between packings. Both of these factors affect packing performance. Another factor in addition to the packing shape and surface area that affects the performance of random or structured packing is the liquid and vapor distribution entering the packed bed. The number of theoretical stages required to make a given separation is calculated using a specific vapor to liquid ratio. If the liquid and vapor are not evenly distributed across the superficial tower area as it enters the packed bed, the liquid to vapor ratio will not be correct in the packed bed and the required separation will not be achieved. The packing will appear to not be working properly. The height equivalent to a theoretical plate (HETP) will be greater than expected. The problem is not the packing itself but the mal-distribution of the fluids entering the packed bed. Liquid mal-distribution is more frequently the problem than vapor. The design of the liquid distributors used to introduce the feed and reflux to a packed bed is critical to making the packing perform to it maximum efficiency. Methods of evaluating the effectiveness of a liquid distributor to evenly distribute the liquid entering a packed bed can be found in references. Considerable work as been done on this topic by Fractionation Research, Inc. (commonly known as FRI).

logo