Plasma seawater purifying equipment

Abstract

The invention discloses plasma seawater purifying equipment. The plasma seawater purifying equipment mainly comprises a seawater plasma supplying network, a first seawater purifying unit, a second seawater purifying unit, a third seawater purifying unit, a fourth seawater purifying unit and a decay nuclear energy online detection instrument, wherein the seawater plasma supplying network, comprisesa sweater supplying network, a seawater evaporation and ionization network, a first seawater boiling and ionization network, a second seawater boiling and ionization network; and the decay nuclear energy online detection instrument is connected to each part and is used for controlling each part to work. The seawater plasma supplying network is used for supplying 106-DEG C seawater plasma gas to the four seawater purifying units through an X-ray photoelectric effect, 106-DEG C plasma is enhanced, multiplied and superimposed by the four seawater purifying units through the X-ray photoelectric effect, ionized oxygen atoms (O<e+>) generate Coulomb repulsion with pollution particles such as heavy metal positive charges so as to purify the seawater, regenerated gas state purified water is collected by virtue of a stainless steel water tank, and regenerated air is discharged into atmosphere.

Description

technical field [0001] The invention belongs to the technical field of seawater purification application, and specifically relates to a plasma purification seawater equipment which utilizes an X-ray source network to ionize seawater into a plasma mixture, purify and restore it with an electrostatic field, and obtain standard drinking water. Background technique [0002] Seawater accounts for 97.5% of global water resources, while terrestrial water resources only account for 2.5% of global water resources. In seawater, the content of salt NaCl(s) is 3%, magnesium chloride MgCl 2 The content of (s) is 0.027%; in addition, seawater also contains bacteria, marine microorganisms, dead bodies of marine organisms and artificial plastic products; organic and inorganic substances discharged by chemical enterprises enter the ocean through lakes and rivers, causing serious organic pollution. and inorganic pollution; heavy metal compounds discharged by non-ferrous metallurgical enterpr...

AI Technical Summary

Problems solved by technology

So far, the main technical features of ordinary physical seawater desalination equipment are: large equipment volume, high power consumption rate, CO 2 (g) Large discharge, low desalination efficiency, bacteria not killed, magnesium chloride MgCl not removed 2 (s) and sulfate SO 4 -2 Sour and bitter impurities, fresh water is bitter; therefore, the fresh water produced by the ordinary physical seawater process is substandard drinking water

At present, common physical seawater desalination equipment mainly has four common physical surface slow evaporation processes: multi-stage flash evaporation, reverse osmosis, multi-effect distillation, and pressure steam distillation; seawater evaporates slowly on the surface, resulting in The volume is particularly large; all kinds of ordinary physical seawater desalination equipment can only use seawater steam H 2 O(g) condenses into liquid water H 2 At O(l), the enthalpy of release becomes heat No X-ray source ( 241 Am, 55 Fe, 238 Pu) performs multiple evaporation ionization and boiling ionization of air and water vapor H 2 O(g), quantum technology that releases bond energy multiple times, resulting in particularly high power consumption of the four major mainstream seawater desalination processes: the basic power consumption of the four major mainstreams is: multi-stage flash evaporation 8.2kwh-9.8kwh / m 3 , reverse osmosis method 6.6kwh / m 3 -9.3kwh / m 3 , multi-effect distillation 7.9kwh / m 3 -10.8kwh / m 3 , Compressed gas distillation 6.6kwh / m 3 -7.1kwh / m 3

The key process of the above-mentioned four major mainstream seawater desalination processes is about 70°C cooling and depressurizing expansion, water molecules H 2 The vaporization of O(l) is carried out slowly on the surface of seawater in the equipment, and salt NaCl(s) and magnesium chloride MgCl 2 Impurities such as (s) and bacteria are left in the evaporation container, which leads to low desalination efficiency and further increase in equipment volume; 2 O(g) and a small amount of NaCl(s) and MgCl 2 (s) and bacteria are brought into the fresh water, resulting in impurities such as salt, magnesium chloride, bacteria and marine microorganisms remaining in the fresh water produced by the seawater desalination process, making the fresh water produced by ordinary physical seawater desalination equipment substandard drinking water

[0004] The heat of vaporization absorbed by the seawater evaporation process water vapor H 2 O(g) condenses into liquid water H 2 The enthalpy change heat released by O(l) The heat released by the two processes is only The heat absorbed by seawater heated from 20°C to 70°C Therefore, for desalinating 1 mol of seawater, ordinary physical seawater desalination equipment must consume about 1.7kJ of electric energy, resulting in a long-term high power consumption rate of ordinary physical seawater desalination processes

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