The article shows how to calculate greenhouse gas emissions of a family and emission reduction activities according to IPCC documents and ISO 14064-1 standards. In this study, direct and energy indirect emissions in 2017 are calculated. Then, within the scope of emission reduction activities, PV system installation, boiler exchange and led conversion are projected. As a result of the calculations, the total emission of the family is found to be 5,331 tons CO 2 -Eq. 84.1% of the total emission is direct emissions that is 4,484 tons CO 2 -Eq. The remaining 15.9% is energy indirect emission that is 0,847 tons CO 2 -Eq. Besides, 0,407 tons CO 2 -Eq from direct emission and 0,464 tons CO 2 -Eq from energy indirect emission are reduced. With the help of simple projections, we can reduce direct emissions by approximately 8%, while energy indirect emissions by about 55%. It is thought that the study will guide the calculation of greenhouse gas emissions and will also help those who wish to reduce greenhouse gas emissions.

No abstract

ÖzYapılan çalışmada kayısı kurutmak için düz ve hapsedici yüzeyli emici plakalara sahip kurutma sistemleri dizayn edilip imalatı yapıldıktan sonra, performansları mukayese edilmiştir. Deneylerde 4-5 mm kalınlığında dilimlenmiş, yaş bazda %76 neme sahip kayısılar kullanılmıştır. Deneylerde 30 dakikalık aralıklarla ölçümler yapılmış ve takip eden ölçümler arasındaki farkın %1'den az olduğu sonuçlarda deney sonlandırılmıştır. Kurutma işlemi, 2,5 , 3,0 ve 3,5 m/s kurutma havası hızlarında gerçekleştirilmiştir. Yapılan deneyler sonucunda, düz yüzeyli kurutma sisteminin kurutma odası ortalama sıcaklığı 45,96 °C iken hapsedici yüzeylinin kurutma odası ortalama sıcaklığı 49,04 °C olarak tespit edilmiştir. Düz yüzeyli kurutma sisteminde tüm hızlarda kurutma süresi 390 dk sürerken hapsedici yüzeyli kurutma sisteminde 2,5 ve 3,0 m/s hızlarında kurutma süresi 330 dk, 3,5 m/s hızda 300 dk sürmüştür. Hapsedici yüzeyli kurutma sisteminin, düz yüzeyli kurutma sistemine göre 2,5 ve 3,0 m/s hızlarda 60 dk, 3,5 m/s hızda 90 dk daha kısa sürede kurutma işlemini gerçekleştirdiği sonucuna varılmıştır. AbstractIn this study, drying systems with flat and incarcerating surface absorbent plates were designed and manufactured for drying apricots, then their performances were compared. Experiments were carried out with slices 4-5 mm thick, with 76% moisture on wet basis. The measurements were made at 30 minute intervals in the experiments and the experiment was terminated when the difference between the following measurements was less than 1%. The drying process was carried out at 2,5, 3,0 and 3,5 m/s drying air velocities. As a result of the experiments, while the average temperature of the drying chamber of the flat surface drying system was found to be 45,96 ° C, the drying chamber average temperature of the incarcerating surface was found to be 49,04 ° C. In the flat surface drying system, the drying time lasts 390 minutes at all speeds, while the drying time of incarcerating surface drying system is 330 minutes at 3,2 and 3,0 m/s and 300 minutes at 3,5 m/s. It has been concluded that the incarcerating surface drying system performs drying at a speed of 2,5 and 3,0 m/s for 60 minutes and 3,5 m/s for 90 minutes shorter than the flat surface drying system.

Bu makaleye şu şekilde atıfta bulunabilirsiniz(To cite to this article): Yatarkalkmaz M. M. ve Özdemir M. B., "Theoretical analysis of a lignite-fired power plant with pre-drying system in terms of energy efficiency and economy",