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500Nm3/H Psa Unit Hydrogen Generator Plant Steam Reforming Unit

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500Nm3/H Psa Unit Hydrogen Generator Plant Steam Reforming Unit

Country/Region china
City & Province chengdu sichuan
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Product Details

500Nm3/H Psa Unit Hydrogen Generator Plant Steam Reforming Unit

 

500Nm3/h Hydrogen Generation Plant,Hydrogen Production From Methanol

 

 

Technology Application

 

Using methanol as raw material, crude hydrogen (mainly CO2, H2, and trace CO, CH4) is produced by steam cracking process, and then purified by pressure swing adsorption technology to obtain hydrogen with purity meeting the requirements of users.
The raw methanol and raw desalted water are premixed at a certain ratio, pressurized by metering pump, preheated, gasified and superheated, and then enter the reactor. Under the action of catalyst, the reaction is carried out to generate crude hydrogen. After heat exchange, the heat is recovered, cooled, and then enter the pressure swing adsorption device for final purification.

 

Diagram of adsorption and separation of gas mixture

 

 

As can be seen from the Langmuir isothermal adsorption equation from, at a certain temperature, the desorption is completed by reducing the pressure. Common desorption methods are atmospheric desorption and vacuum desorption, which purpose is to reduce the partial pressure of adsorbate. The adsorption and desorption of as shown in the illustration:

Pressure swing adsorption (PSA) and temperature swing adsorption (TSA) purification process is realized by two properties of adsorbent in the physical adsorption: one is the different adsorption capacity of different components, the two is the adsorption capacity of adsorbate on the adsorbent increases with partial pressure and decrease with increasing adsorption temperature. The first property of the adsorbent, may realize the preferential adsorption of impurity components containing in hydrogen syn-gas for hydrogen purification purposes; for the second property, can achieve adsorbing at high pressure and low temperature, desorbing in low pressure and high temperature. This cycle of adsorption and regeneration achieve the purpose of continuous hydrogen purification. But decrease with increasing adsorption temperature.

 

Serial numberProject name and scaleConstruction siteTime
Methanol conversion - PSA hydrogen generation
11

150Nm³/h Methanol conversion-PSA hydrogen generation

modified to 250Nm³/h

Taizhou, Zhejiang2011
12200Nm³/h Methanol conversion-PSA hydrogen generation

Hebei Qian'an

(high purity hydrogen)

2013
13250Nm³/h Methanol conversion-PSA hydrogen generationFuzhou, Fujian2011
14250Nm³/h Methanol conversion-PSA hydrogen generationHenan Puyang2012
15300Nm³/h Methanol conversion-PSA hydrogen generationFujian Xiamen2005
16300Nm³/h Methanol conversion-PSA hydrogen generationSichuan Yibin2006
17300Nm³/h Methanol conversion-PSA hydrogen generationIndonesia2006
18300Nm³/h Methanol conversion-PSA hydrogen generationJiangsu Zhangjiagang2006
19300Nm³/h Methanol conversion-PSA hydrogen generationShandong Yucheng2006
20300Nm³/h Methanol conversion-PSA hydrogen generationHebei Zhaozhou2007
21300Nm³/h Methanol conversion-PSA hydrogen generationShandong Yucheng2010
22300Nm³/h Methanol conversion-PSA hydrogen generationHebei Cangzhou2010
23300Nm³/h Methanol conversion-PSA hydrogen generationZhejiang Xianju2012
24300Nm³/h Methanol conversion-PSA hydrogen generationHebei Handan2012
25300Nm³/h Methanol conversion-PSA hydrogen generationShandong Dongying2013
26300Nm³/h Methanol conversion-PSA hydrogen generationSichuan Suining2013
27400Nm³/h Methanol conversion-PSA hydrogen generationJiangsu Rugao2007
28400Nm³/h Methanol conversion-PSA hydrogen generationGuangdong Zhaoqing2008
29400Nm³/h Methanol conversion-PSA hydrogen generationJilin Gongzhuling2008
30400Nm³/h Methanol conversion-PSA hydrogen generationHenan Xinxiang2006

 

Technical indexes

 

Capacity:500Nm3/h
Purity:99% ~ 99.999%

 

Features and advantages

 

Mature process technology and safe and reliable operation.
Wide source of raw material and large processing scale.
Advanced recovery technology of thermal energy and low consumption of production energy.

 

Reference

 

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