Ultra-pure ammonia production device and production method
A production device and technology for ultra-pure ammonia, applied in separation methods, chemical instruments and methods, ammonia compounds, etc., can solve the problems of limited production of ultra-pure ammonia and high energy consumption, and achieve production cost savings, low energy consumption, The effect of improving the removal rate
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Embodiment 1
[0048] A kind of ultra-pure ammonia production device, the structure is as follows figure 1 As shown, it includes two parallel evaporator groups 1 (one for use and one for standby), a heating system 2 , a partition tower 3 and a parallel adsorption-desorption device 7 . Each group of evaporators 1 is composed of two evaporators 11 in series, each evaporator 11 is provided with a packing layer 8 (stainless steel wire mesh) on the upper part, and the adjacent two evaporators 11 are connected through the overflow series pipe 4, The overflow series pipeline 4 is provided with a return liquid port 41, and the return liquid port 41 communicates with the top of the first evaporator 11; the lower part of the side wall of each evaporator 11 is provided with a liquid ammonia feed port 111; each evaporator The bottom of 11 is provided with the first heavy component discharge port 112; The top of each evaporator 11 is provided with the first light component discharge port 113; The heating...
Embodiment 2
[0059] It differs from Embodiment 1 in that each evaporator group 1 is composed of eight evaporators 11 connected in series, and other devices and their connections are the same. The specific process control situation of using the ultrapure ammonia production device of the present embodiment to produce ultrapure ammonia is as follows:
[0060] Composition of raw material liquid anhydrous industrial ammonia: moisture 0.1%, oil content 5mg / kg, iron content 1mg / kg, methane 0.099%, ethane 0.0005%, propane 0.0004%, of which ammonia content is 99.9%; liquid ammonia flow rate is 347kg / h;
[0061] Evaporator 11: diameter D=500mm, height H=800mm, temperature inside evaporator 11 is 10~40℃, pressure is 0.1~2kPaG; after one separation, the composition of the first light component is: water 0.16%, oil content of 0.3mg / kg, iron content of 0.3mg / k, methane content of 0.123%, ethane content of 0.0006%, propane content of 0.0003%, and ammonia content of 99.99%;
[0062] Heating system 2, t...
Embodiment 3
[0065] It differs from Embodiment 1 and Embodiment 2 in that each evaporator group 1 is composed of 12 evaporators 11 connected in series, and other devices and their connections are the same. The specific process control situation of using the ultrapure ammonia production device of the present embodiment to produce ultrapure ammonia is as follows:
[0066] Composition of raw material liquid anhydrous industrial ammonia: moisture 0.36%, oil content 14mg / kg, iron content 1.1mg / kg, methane 0.095%, ethane 0.0011%, propane 0.0013%, of which ammonia content is 99.7%; liquid ammonia flow rate is 500kg / h;
[0067] Evaporator 11: diameter D=500mm, height H=800mm, temperature inside evaporator 11 is 10~40℃, pressure is 0.1~2kPaG; after one separation, the composition of the first light component is: water 0.53%, oil content of 1.4mg / kg, iron content of 0.2mg / kg, methane content of 0.175%, ethane content of 0.0029%, propane content of 0.0011%, and ammonia content of 99.91%;
[0068] H...
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