﻿ 渣浆泵的特性曲线分析_公司新闻_河北沐阳泵业安徽快3开奖结果

# 安徽快3开奖结果

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1.扬程一流量曲线
由欧拉公式可得无限多叶片假设条件下的理论扬程见式(1-16)。在离心泵中,叶轮叶片的出口角一般小于90°。若以流量为横坐标扬程为纵坐标,则Hx-Qr为一向下倾斜的直线(1-29曲线1)

H-Qt线(曲线4)上工况点C为例，过C点作水平线与H -q线(曲线8)交于点A,与纵坐标交于点B,AB线段的长度即为C点扬程所对应的泄漏量q。将C点向左平移q得到D,D即为考虑流量泄漏损失后的工况点。从流量一扬程曲线HQT的横坐标数值中减去相应的泄漏量q，就可得到泵的流量一扬程曲线 H - Q线(曲线5)渣浆泵
由以上分析可知，H-Q曲线的形状与叶轮的圆周速度u2、外径D2和叶片角以及各种阻力损失密切相关。

Characteristic curve analysis of slurry pump

The relationship curves of the head and flow, power and flow, efficiency and flow, and suction vacuum (or necessary cavitation) and flow of a centrifugal pump at a certain speed are called the working characteristic curves of the pump, which can reflect the performance characteristics of the pump.

According to Euler's formula, the theoretical lift of infinite blades under the assumption is shown in formula (1-16). In centrifugal pump, the outlet angle of impeller blade is generally less than 90 °. If the flow is taken as the abscissa and the lift as the ordinate, HX QR is a straight line inclined downward (Fig. 1-29 curve 1).

It can be seen from formula (1-21) that under the condition of limited number of blades in centrifugal pump, the theoretical head is HT = phro, and the slip coefficient of centrifugal pump is independent of flow, i.e., μ is constant. -The longitudinal coordinates of each point on Q1 (curve 1) are multiplied by μ. Since the value of slip coefficient μ is less than 1, the theoretical head hr-q τ relation curve (curve 2) of centrifugal pump with limited number of blades can be obtained. Since the energy head of the actual liquid is h = HT HF sh, the friction loss HF corresponding to the same flow rate is subtracted from the theoretical head hr-qt (curve 2), and then the curve 3 is obtained, and the impact loss SH is subtracted, then the relationship between the actual head and flow h-qr (curve 4) can be obtained.

Take point C on h-qt line (curve 4) as an example, cross point C as horizontal line and H-Q line (curve 8) to point a, and cross point B with ordinate。 The length of line AB is the leakage Q corresponding to the lift of point C。 Translate point C to the left and Q to get D。 point D is the operating point after considering the loss of flow leakage。 By subtracting the corresponding leakage Q from the abscissa value of the flow head curve h-qt, the flow head curve H-Q line (curve 5) of the pump can be obtained。 Slurry pump

It can be seen from the above analysis that the shape of H-Q curve is closely related to the peripheral velocity U2, outer diameter D2, blade angle and various resistance losses of impeller.