C01B7/14

PREPARATION METHOD AND USE OF AN ATOMIC-STATE FLUID IODINE AND ITS DERIVED NANO-IODINE

In one aspect, the present disclosure belongs to the new material field and can be used to produce atomic-state fluid iodine by iodine atom rearrangement occurring in the pseudo-critical reaction system. In one aspect, the atomic-state fluid iodine has a specific gravity of about 3.8-4.0 g/mL and maintains stable physical state under 10-100 C and light environment without sublimation or decomposition. As a new-type iodine-structural material, atomic-state fluid iodine and atomic-state nano-iodine can be used as the 4.sup.th generation of atomic-state iodine disinfectant for human, animal and living environment, experimental data show that as atomic-state germicide in agricultural production, it can prevent and cure specific parasitism disease of plant, such as Citrus Huanglongbing and citrus bacterial canker disease, banana panama disease, fruit tree branch blight disease and plant virus disease, and it can also be used as a substitution in medical and health field for its features of safety, stability and high potency.

PREPARATION METHOD AND USE OF AN ATOMIC-STATE FLUID IODINE AND ITS DERIVED NANO-IODINE

In one aspect, the present disclosure belongs to the new material field and can be used to produce atomic-state fluid iodine by iodine atom rearrangement occurring in the pseudo-critical reaction system. In one aspect, the atomic-state fluid iodine has a specific gravity of about 3.8-4.0 g/mL and maintains stable physical state under 10-100 C and light environment without sublimation or decomposition. As a new-type iodine-structural material, atomic-state fluid iodine and atomic-state nano-iodine can be used as the 4.sup.th generation of atomic-state iodine disinfectant for human, animal and living environment, experimental data show that as atomic-state germicide in agricultural production, it can prevent and cure specific parasitism disease of plant, such as Citrus Huanglongbing and citrus bacterial canker disease, banana panama disease, fruit tree branch blight disease and plant virus disease, and it can also be used as a substitution in medical and health field for its features of safety, stability and high potency.

Method of adsorbing iodine or bromine

The present invention relates to an iodine (I.sub.2) or bromine (Br.sub.2) adsorbent including a zeolite having a Si/Al ratio of 15 or greater; an I.sub.2 or Br.sub.2 carrier including the I.sub.2 or Br.sub.2 adsorbent; a column filled with the I.sub.2 or Br.sub.2 adsorbent; a article composed of the I.sub.2 or Br.sub.2 adsorbent or having the I.sub.2 or Br.sub.2 adsorbent attached thereto; a method for adsorbing or removing I.sub.2 or Br.sub.2 using the I.sub.2 or Br.sub.2 adsorbent; an iodine- or bromine-containing zeolite composite including a porous zeolite and iodine (I.sub.2) or bromine (Br.sub.2) confined in the pores of the zeolite; a semiconductor material including the iodine- or bromine-containing zeolite composite; and a method for preparing an iodine- or bromine-containing product using the iodine- or bromine-containing zeolite composite.

Method of adsorbing iodine or bromine

The present invention relates to an iodine (I.sub.2) or bromine (Br.sub.2) adsorbent including a zeolite having a Si/Al ratio of 15 or greater; an I.sub.2 or Br.sub.2 carrier including the I.sub.2 or Br.sub.2 adsorbent; a column filled with the I.sub.2 or Br.sub.2 adsorbent; a article composed of the I.sub.2 or Br.sub.2 adsorbent or having the I.sub.2 or Br.sub.2 adsorbent attached thereto; a method for adsorbing or removing I.sub.2 or Br.sub.2 using the I.sub.2 or Br.sub.2 adsorbent; an iodine- or bromine-containing zeolite composite including a porous zeolite and iodine (I.sub.2) or bromine (Br.sub.2) confined in the pores of the zeolite; a semiconductor material including the iodine- or bromine-containing zeolite composite; and a method for preparing an iodine- or bromine-containing product using the iodine- or bromine-containing zeolite composite.

Iodine extraction processes

Processes for extracting iodine from an aqueous solution, such as brine, are disclosed. Activated coconut carbon particles are mixed with the solution to adsorb iodide through pores in the activated carbon particles. The activated carbon particles are then treated with sulfur dioxide gas and water to form hydrogen iodide. The hydrogen iodide is then reacted with chloride to obtain elemental iodine (I.sub.2).

Iodine extraction processes

Processes for extracting iodine from an aqueous solution, such as brine, are disclosed. Activated coconut carbon particles are mixed with the solution to adsorb iodide through pores in the activated carbon particles. The activated carbon particles are then treated with sulfur dioxide gas and water to form hydrogen iodide. The hydrogen iodide is then reacted with chloride to obtain elemental iodine (I.sub.2).

Production method for particles of element having standard electrode potential greater than 0V
09928945 · 2018-03-27 · ·

The present invention provides: a method for producing particles of an element having a standard electrode potential greater than 0V, characterized by using in a protic solvent solution a polysilane having a poor solubility in an aprotic solvent, to produce particles of the element from ions of at least one element having a standard electrode potential greater than 0V; and a composite body of polysilane and the particles of an element having a standard electrode potential greater than 0V, in which the particles of the at least one element having a standard electrode potential greater than 0V (provided that palladium is not included in the element, in the case where the polysilane is a dimethyl polysilane) are adsorbed in the polysilane having poor solubility in an aprotic solvent.

Production method for particles of element having standard electrode potential greater than 0V
09928945 · 2018-03-27 · ·

The present invention provides: a method for producing particles of an element having a standard electrode potential greater than 0V, characterized by using in a protic solvent solution a polysilane having a poor solubility in an aprotic solvent, to produce particles of the element from ions of at least one element having a standard electrode potential greater than 0V; and a composite body of polysilane and the particles of an element having a standard electrode potential greater than 0V, in which the particles of the at least one element having a standard electrode potential greater than 0V (provided that palladium is not included in the element, in the case where the polysilane is a dimethyl polysilane) are adsorbed in the polysilane having poor solubility in an aprotic solvent.

Subterranean Well Production Saltwater Evaporation Station with Saltwater Recycle
20170114271 · 2017-04-27 ·

A process comprising spraying production saltwater comprising water and dissolved salt through an evaporator to evaporate a portion of the water, collecting unevaporated saltwater which is an unevaporated portion of the saltwater that remains after being sprayed through the evaporator, and adjusting a salinity of at least a portion of the unevaporated saltwater to yield an adjusted brine product.

PURIFICATION OF NACL BRINE CONTAINING IODINE
20170096346 · 2017-04-06 ·

The present invention provides a process for separating iodine from a NaCl brine, comprising the following steps: (a) providing said NaCl brine containing iodide, (b) adjusting the pH of said NaCl brine to be no greater than 1.5, (c) adding oxidizing agent, such as chlorine containing oxidizing agent, to said NaCl brine resulting from step (b) to obtain an oxidation-reduction potential in said NaCl brine of from 560 mV to 925 mV, the combination of said pH of no greater than 1.5 and oxidation-reduction potential of 560 mV to 925 mV resulting in the formation of an iodine-chlorine anionic complex, and (d) contacting nonionic adsorption resin and said NaCl brine from step (c) one with the other to adsorb said iodine from this brine, to obtain as a result thereof NaCl brine wherein the iodine content therein is preferably no greater than 100 ppbw, more preferably no greater than 10 ppbw.