CN1506315A

CN1506315A - Prepn of laminated dihydrogen oxide and its derivative quasi-periclase

Info

Publication number: CN1506315A
Application number: CNA021485224A
Authority: CN
Inventors: 陈天虎
Original assignee: Hefei University of Technology
Current assignee: Hefei University of Technology; Hefei Polytechnic University
Priority date: 2002-12-10
Filing date: 2002-12-10
Publication date: 2004-06-23
Anticipated expiration: 2022-12-10
Also published as: CN1208125C

Abstract

The present invention features that by using industrial acid waste water and inorganic salt in waste liquid as material and through inorganic chemical reaction, laminated dihydroxide (LDH) is synthesized; and through high temperature calcination, the derivative quasi-periclase is produced. The present invention is one new waste water processing technology and new LDH synthesizing technology for processing waste water and preparing LDH simultaneously. The prepared LDH or derivative quasi-periclase may be used as water purifying agent for processing waste water and drinking water. The present invention realizes the comprehensive waste treatment and resource utilization.

Description

Layered double-hydroxide and derivative thereof are like the preparation method of periclasite

Technical field:

The present invention relates to nonmetal mineral resource deep processing, inorganic chemical industry and field of environment engineering technology.Layered double-hydroxide and derivative thereof the preparation method like periclasite more specifically says so.

Background technology:

Layered double-hydroxide (layer double hydroxide is called for short LDH) claims anionic clay (anion clay) again, claims again like talcum (talcite-like), hydrotalcite (hydrotalcire is called for short HTs).Its basic structure formula is: M _x ²⁺M _y ³⁺(OH) _2x+3y-nz(A ^N-) mH ₂O, M ²⁺And M ³⁺Represent divalence and Tricationic respectively, A ^N-Represent n valency negatively charged ion.LDH has the laminate structure of similar water magnesite, and in the structural unit layer of brucite, the divalent cation part is substituted by the trivalent negatively charged ion, produces the structure positive charge.Thereby need to introduce negatively charged ion and enter structural unit interlayer balanced structure positive charge.Similar with general clay mineral, the negatively charged ion and the structure positive charge that are between structural sheet belong to long-range electrostatic balance, reactive force a little less than, negatively charged ion wherein can be by other anionresin, thereby LDH has excellent the moon from switching performance.

The lasting focus of studying over LDH research becomes surplus the international material science nearly 10 year, its key are that the composition of LDH can regulate and control in a big way, the special structure and the material of this structure have some special nature and have a wide range of applications.The application of LDH in environmental protection is all good Application Areas of foreign scholar, utilized LDH to make the transition-metal catalyst of spinel structure as the pioneer at present.LDH has also been carried out more research as water treatment absorbent, demonstrate very large prospect, the high price oxo-anions of particularly doing in sorbent treatment waste water and the tap water such as phosphate radical, arsenate, selenate radical, chromate, sulfate radical demonstrates good effect.The problem that exists mainly is that the LDH that the investigator prepares is the preparation that chemical reagent is finished under strict experiment condition mostly at present, and the technology of research can not be amplified, and turnout is little, and the cost height is difficult in the actual waste water processing and uses.Thereby although the discovery of LDH, study the history of decades, synthetic technology research has also formed more achievement, and LDH is used as water treatment absorbent, remains the problem in Technological Economy.

Summary of the invention:

Technical problem to be solved by this invention is to avoid above-mentioned existing in prior technology weak point, and a kind of layered double-hydroxide and derivative thereof the preparation method like periclasite is provided.Be to be effective constituent with the inorganic salts in various industrial acidic wastewaters, the waste liquid, preparation can be used for the LDH product in fields such as waste water, drinking water treatment when handling waste water, waste liquid, reaches the treatment of wastes with processes of wastes against one another, the purpose of comprehensive utilization of resources.

The technical scheme that technical solution problem of the present invention is adopted is:

Technical characterstic of the present invention is that layered double-hydroxide is to be effective constituent with the inorganic salts in industrial acidic wastewater, the waste liquid, through the synthetic preparation of inorganic chemistry reaction and get.

The derivative of layered double-hydroxide of the present invention is to form with prepared layered double-hydroxide high-temperature calcination like the preparation characteristic of magnesite.

Compared with the prior art, beneficial effect of the present invention is embodied in:

The present invention is to be effective constituent with the inorganic salts in various industrial acidic wastewaters, the waste liquid, prepares LDH when handling waste water, waste liquid.Being a wastewater treatment new technology, is again a LDH new synthesis technology.Prepared LDH or deutero-can be used as the scavenging agent of other industry waste water and drinking water treatment like the periclasite material, reach the treatment of wastes with processes of wastes against one another, comprehensive utilization of resources.Because technology of the present invention is to be purpose with the wastewater treatment, takes into account the preparation of LDH, thereby LDH that produces and derived product thereof is cheap, is suitable for practicality.

Fig. 1 is the X-ray powder diffraction pattern.

Fig. 2 is with the synthetic LDH transmission electron microscope image of activated clay production waste.

Fig. 3 is the X-luminous energy spectrogram of synthetic LDH.

Fig. 4 is calcining LDH transmission electron microscope image.

Fig. 5 is the X-luminous energy spectrogram of calcining LDH.

Fig. 6 technological process of production synoptic diagram of the present invention.

Embodiment:

The preparation of the layered double-hydroxide in the present embodiment is to be effective constituent with the inorganic salts in industrial acidic wastewater, the waste liquid.

Waste water, waste liquid that present embodiment is suitable for comprise: with wilkinite, attapulgite clay is waste water, the waste liquid of raw material production atlapulgite, white carbon black, the bittern that evaporation salt is produced, pickling waste waters, waste liquid.From chemical ingredients, comprise: contain Mg ²⁺, Al ³⁺, Cu ²⁺, Co ²⁺, Ni ²⁺, Fe ²⁺, Fe ³⁺Waste water, waste liquid.Adding reaction mass should make Mg/Al in the reaction vessel, Cu/Al, Co/Al, Ni/Al ratio at 4: 1～1: 1.

For being waste water, the waste liquid of raw material production atlapulgite, active silica with wilkinite, attapulgite clay, the reaction mass that synthetic LDH adds is a carbonatite, be Wingdale, dolomite, or contain other material of rhombspar, calcite, or lime, Calcareous material, or be caustic soda and the solution that contains caustic soda.And the selection by material and coupling satisfy in the reaction vessel Mg/Al ratio at 4: 1～1: 1.Optimum ratio was at 2: 1.

For main magniferous salts solution of bittern class or waste liquid, and contain Cu ²⁺, Co ²⁺, Ni ²⁺Waste water, waste liquid, the reaction mass that synthetic LDH adds can be basic aluminium salt solution or waste liquids such as sodium metaaluminate, or caustic soda and the solution that contains caustic soda.Keep Mg/Al in the reactor (at containing magnesium solution, waste water) or Cu/Al (at copper-containing wastewater) or Co/Al (at cobalt-containing wastewater) or Ni/Al (at nickel-containing waste water) ratio and maintain 4: 1～between 1: 1.Optimum ratio is 2: 1.

In concrete the enforcement, control the LDH building-up reactions by control reaction end pH value, endpoint pH is between 8～10, and optimum value is 8.5.Terminal point pH can influence divalent cation and the ratio of Tricationic and the performance of layered double-hydroxide in the synthetic product.

Reach the well-crystallized of LDH by high degree of agitation, control reaction temperature.Wherein, temperature of reaction is at 10-95 ℃

Preparing its derivative like magnesite with prepared layered hydroxide, is to form by high-temperature calcination.Calcining temperature is 200-600 ℃.

The concrete technological process of production as shown in Figure 6.

The LDH building-up reactions feeds intake and should form different raw materials according to waste water, waste liquid character, prepares multi-form LDH product, and has different application.

Extremely shown in Figure 5 by Fig. 1, utilize the modern structure analysis means to find that LDH forms the seemingly porous oxide of the nanometer grade of periclasite structure at suitable temperature lower calcination, have greater activity, aquation formation is the novel LDH of interlayer anion with the hydroxyl again in the aqueous solution.This new life's of aquation again LDH has better ion-exchange performance, and this shows that also LDH can obtain regeneration by this mode.

Has as shown in Figure 1 X-ray powder diffraction with the inventive method synthetic LDH and calcinate.Among the figure, TT-LDH-60: attapulgite clay is that raw material production atlapulgite waste water prepares LDH.TT-LDH-300: by the LDH 300 degree calcinates of waste water preparation---like the periclasite structure.

In addition, have as Fig. 2 to tabular crystal form shown in Figure 5 with the inventive method synthetic LDH and calcinate.

Claims

1, the preparation method of layered double-hydroxide is characterized in that with the inorganic salts in industrial acidic wastewater, the waste liquid be effective constituent, gets through the synthetic preparation of inorganic chemistry reaction.

2, the preparation method of layered double-hydroxide according to claim 1 is characterized in that described industrial acidic wastewater is for containing Mg ²⁺, or Al ³⁺, or Cu ²⁺, or Co ²⁺, or Ni ²⁺, or Fe ²⁺, or Fe ³⁺Waste water or waste liquid.

3, the preparation method of layered double-hydroxide according to claim 2 is characterized in that concrete preparation process is:

A, add the ratio that reaction mass comes Mg/Al in the controlling reactor, Cu/Al, Co/Al, Ni/Al, make them at 4: 1～1: 1, building-up reactions is finished under high degree of agitation;

B, control reaction end pH value are between 8～10;

C, control reaction temperature reach the well-crystallized of LDH, temperature of reaction 10-95 ℃;

D, solid-liquid separation, washing;

E, solid product drying, dispersion, packing are gained layered double-hydroxide product.

4, the preparation method of layered double-hydroxide according to claim 3, it is characterized in that described industrial acidic wastewater, waste liquid are with wilkinite, or attapulgite clay is waste water, the waste liquid of raw material production atlapulgite, active silica, the reaction mass that synthetic LDH adds is a carbonatite, or contain rhombspar, calcite material, or lime and Calcareous material, or be caustic soda and the solution that contains caustic soda.

5, the preparation method of layered double-hydroxide according to claim 3 is characterized in that described industrial acidic wastewater, waste liquid are main magniferous salts solution of bittern class or waste liquid, contain Cu ²⁺, Co ²⁺, Ni ²⁺It is basic aluminium salt solution or waste liquids such as sodium metaaluminate that waste water, waste liquid, synthetic LDH add reaction mass, or caustic soda and the solution that contains caustic soda.

6, a kind of derivative of layered double-hydroxide is characterized in that forming with the prepared layered hydroxide high-temperature calcination of claim 1 like the preparation method of periclasite.

7, the preparation method like periclasite according to claim 5 is characterized in that calcining temperature is 200-600 ℃.