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潜水渣浆泵扬程低的原因及解决办法
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 潜水渣浆泵在运用的过程中,会呈现扬程低这种缺点,那么招致渣浆泵扬程低的缘由是什么呢?有什么办法处置呢?下面我们就一同来看看吧:

  扬程低的缘由:
  1、吸入管路系统进气;
  2、吸入管路或叶轮堵塞;
  3、潜水渣浆泵进口阀门没有展开或阀门已损坏构成泵气蚀;
  4、泵扬程低于管路理论扬程,而构成泵流量小;
  5、管路汽蚀余量小于潜水渣浆泵须汽蚀余量构成泵量小;
  6、渣浆浓度太大。
  处置办法:
  1、扫除进气缘由;
  2、降低渣浆泵渣浆浓度或换大一规格口径的泵;
  3、展开进口阀门或改换新阀门;
  4、进步潜水渣浆泵扬程;
  5、扫除堵塞;
  6、造管路装置,使管路汽蚀余量大于泵需汽蚀余量或换汽蚀性能满足管路装置恳求的泵。
  置信经过文章的阅读,假设大家再遇上潜水渣浆泵扬程低的时分就不会手足无措了吧。多控制一些设备的学问,会在关键时辰辅佐到大家的。
In the process of using the submersible slurry pump, the fault of low head will appear. What is the reason for the low head of the slurry pump? What is the solution? Let's take a look:
Reasons for low lift:
1. Intake pipe system;
2. The suction pipeline or impeller is blocked;
3. The inlet valve of submersible slurry pump is not expanded or the valve has been damaged, resulting in pump cavitation;
4. The pump head is lower than the actual head of the pipeline, resulting in small pump flow;
5. The NPSH of the pipeline is less than that of the submersible slurry pump, resulting in small pump volume;
6. The concentration of slag slurry is too high.
terms of settlement:
1. Eliminate the cause of air intake;
2. Reduce the slurry concentration of the slurry pump or change the pump with a larger diameter;
3. Expand the inlet valve or replace it with a new one;
4. Increase the head of submersible slurry pump;
5. Remove blockage;
6. Build pipeline devices so that the NPSH of the pipeline is greater than the NPSH required by the pump, or replace the pump whose NPSH performance meets the requirements of the pipeline device.
I believe that through reading the article, if you encounter the low head of submersible slurry pump again, you won't be at a loss. Mastering more equipment knowledge will help you at the critical moment.