Table 1 shows the experimental cond

Table 1 shows the experimental conditions and Fig. 7 displays the bias in the previous study by Kim and Kim (2012) and the evaporator secondary fluid inlet temperature is 27 C. The error bars at each point represent ±dCOP which means uncertainty for each point. The controller adjusts the heat rejection pressure so that the system becomes to be operated at the point where COP line and dq_=dw_ line cross.
ตารางที่ 1 แสดงเงื่อนไขทดลอง และ Fig. 7 แสดงความโน้มเอียงในการศึกษาก่อนหน้านี้โดยคิมคิม (2012) และอุณหภูมิทางเข้าของของเหลวรอง evaporator 27 C. แถบข้อผิดพลาดในแต่ละจุดแทน ±dCOP ซึ่งหมายถึง ความไม่แน่นอนแต่ละจุด ตัวควบคุมปรับความดันปฏิเสธความร้อนเพื่อให้กลายเป็นระบบการดำเนินการ ณจุดที่COPและ ข้ามสายdq_ = dw_

ผลลัพธ์ (อังกฤษ) 1:

Table 1 shows the experimental conditions and Fig. 7 displays the bias in the previous study by Kim and Kim (2012) and the evaporator secondary fluid inlet temperature is 27 C. The error bars at each point represent ±dCOP which means uncertainty for each point. The controller adjusts the heat rejection pressure so that the system becomes to be operated at the point where COP line and dq_=dw_ line cross.Table 1 shows the experimental conditions and Fig. 7 shows a bias in previous scholarship by khimkhim (2012) and the secondary fluid inlet temperature evaporator 27 C. error bars in each point represents ± dCOP, which means uncertainty for each point. Pressure adjustment controls rejection heat in order to become an operation system. The nachut COP and cross the line of dq _ = dw_

ผลลัพธ์ (อังกฤษ) 2:

Table 1 shows the experimental conditions and Fig. 7 displays the bias in the previous study by Kim and Kim (2012) and the evaporator secondary fluid inlet temperature is 27 C. The error bars at each point represent ± dCOP which means uncertainty for each point. . The controller adjusts the heat rejection pressure so that the system becomes to be operated at the point where COP line and dq_ = dw_ line cross.
Table 1 shows the conditions trials and Fig. 7 shows an inclination to study previously. Kim (2012) and the temperature of the liquid in the secondary evaporator 27 C. Error bars represent ± dCOP which each point represents the uncertainty for each point. Control pressure heat rejection to the system operation. At that point, COP and cross-dq_ = dw_.

ผลลัพธ์ (อังกฤษ) 3:

Table 1 shows the experimental conditions and Fig. 7 displays the bias in the previous study by Kim and Kim (2012 and.) The evaporator secondary fluid inlet temperature is 27 C. The error bars at each point represent edge dCOP which means uncertainty. For each point.The controller adjusts the heat rejection pressure so that the system becomes to be operated at the point where COP line. And DQ _ = DW _ line cross.
Table 1 show condition experiment and Fig. 7 show inclination in earlier studies by Kim Kim (2012) and temperature of liquid secondary entrance Evaporator 27 C.Error bar on each point. The edge dCOP which means uncertainty each point. Control pressure adjustment rejected heat to become a system operation. At that point COP and crossed the DQ _ = DW _
.