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CN1095388C - Dechlorinating agent and its preparing method - Google Patents

Dechlorinating agent and its preparing method Download PDF

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Publication number
CN1095388C
CN1095388C CN98121676A CN98121676A CN1095388C CN 1095388 C CN1095388 C CN 1095388C CN 98121676 A CN98121676 A CN 98121676A CN 98121676 A CN98121676 A CN 98121676A CN 1095388 C CN1095388 C CN 1095388C
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CN
China
Prior art keywords
dechlorinating agent
dechlorinating
agent
hours
water
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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CN98121676A
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Chinese (zh)
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CN1223898A (en
Inventor
李新怀
袁友明
吕小婉
李耀会
马溪生
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Huashuo Technology Co., Ltd.
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HUBEI RESEARCH INSTITUTE OF CHEMISTRY
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Abstract

The present invention provides a dechlorinating agent and a preparation method thereof. Calcium compounds, sodium compounds, aluminum hydroxide and iron hydroxide are used as active components; inorganic clay and bentonite are used as carriers, or colloid SiO2 and a hole expansion agent are also added; the dechlorinating agent is prepared by the drying at the temperature from 80 to 120 DEG C and the calcining at the temperature from 300 to 400 DEG C after mixed mulling for strip squeezing; the dechlorinating agent respectively has the components of the following weight percentage measured according to the oxides of 10 to 40% of CaO, 10 to 23% of Na2O, 5 to 11% of Al2O3, 11 to 24% of Fe2O3, 10 to 40% of inorganic bentonite, colloid SiO2 accounting for 0 to 5% of the weight of the matching materials and hole expansion agent accounting for 0 to 5% of the weight of the matching materials. The dechlorinating agent of the present invention has the advantages that low cost of raw materials and easy obtainment of the raw materials; HCl in gases can be lowered to be below 0.1 ppm from 1000 ppm, the penetration chlorine capacity reaches 40 to 50 m% at the moment, and the water-resistant performance is good. The present invention can be widely used for dechlorinating various gases in petrochemical industry and chemical fertilizer industry.

Description

Dechlorinating agent and preparation method thereof
The invention belongs to gas purifying agent that removes hydrogenchloride in the material gas and preparation method thereof.
In chemical fertilizer industry and petrochemical complex production, for various reasons, more or less contain hydrogen chloride impurity in the unstripped gas.Hydrogenchloride very easily causes the poisoning of catalyst inactivation to the toxic effect of many effective catalysts, goes back corrosive equipment simultaneously, generates the salt blocking pipeline, usually is forced to subtract car, parking because of the harm of chlorine in the production, has had a strong impact on ordinary production.
Be head it off, must effectively remove the hydrogenchloride in the unstripped gas, in both at home and abroad developing the different dechlorinating agent of many performances in succession and being applied to produce.US4762537 utilizes activated alumina and Y zeolite to handle the hydrogeneous reformed gas of HCl less than 100ppm.US4639259 loads on alkaline-earth metal on the aluminum oxide with X-ρ-η phase structure, and the chlorosity amount can reach 13.8m%, and degree of purification is less than 1ppm.US3935295 then adopts Ca (OH) 2Mix with ZnO, be extruded into bar, can remove micro-chlorine and a small amount of hydrogen sulfide, average chlorosity reaches 23.6m%.Publication number CN1064099A as active ingredient, sneaks into the natural inorganic clay with basic metal and alkaline-earth metal, HCl in the unstripped gas can be taken off to 0.5ppm, and the chlorosity amount reaches 35.2m%.Publication number CN1147977 then introduces zn cpds again in basic metal or alkaline-earth metal, chlorine in the unstripped gas can be removed to below the 0.1ppm, and the chlorosity amount reaches 30m%.In addition, adopt CuO-ZnO/Al in addition 2O 3The dechlorinating agent of component, the chlorosity amount is less than 15m%.Though dechlorinating agent kind and performance have had very great development more in early days, still need improve raising on degree of purification, water resistance.
The object of the present invention is to provide a kind of new dechlorinating agent and preparation method thereof, this dechlorinating agent raw material is easy to get and prepares easily, and cost is low and degree of purification is good, the chlorosity height, and water resistance is good, and the HCl that is used for petrochemical complex and the various chloride unstripped gass of chemical fertilizer industry removes.
Technical scheme of the present invention is: remove that the dechlorinating agent of hydrogenchloride is to contain calcium cpd such as CaO, sodium compound such as NaHCO in the material gas 3, Na 2CO 3, ironic hydroxide Fe (OH) 3, and aluminium hydroxide γ-AlOOH active constituent, the inorganic clay wilkinite carrier that form, wherein, the weight percentage of each component is respectively CaO 10-40%, Na by oxide compound 2O 10-23%, Al 2O 35-11%, Fe 2O 311-24%, inorganic bentonite 10-40%.
In dechlorinating agent of the present invention, have better intensity and water tolerance in order to make it, can in active constituent and carrier, add the colloid SiO of component weight percentage 0-5% 2, form more porous road in order to make dechlorinating agent inside, help the carrying out of mass transfer, improve chlorosity, can in active constituent and carrier, add a certain amount of expanding agent NH 4HCO 3Or urea, the addition of expanding agent is the 0-5% of batching overall weight percent.
Preparation method's step of this dechlorinating agent is:
1, ironic hydroxide is added water or also add the colloid SiO of proportional quantity 2With expanding agent NH 4HCO 3Or urea stirs into suspension:
2, calcium oxide, yellow soda ash or sodium bicarbonate, aluminium hydroxide γ-AlOOH and the wilkinite mixed grind of adding proportional quantity become paste in above-mentioned suspension, place this paste more than 4 hours;
3, with behind the 2 gained paste extruded mouldings in 80-120 ℃ of drying more than 2 hours, again 300-400 ℃ of roasting more than 2 hours promptly.
This dechlorinating agent side pressure strength is greater than 50N/cm.
It is soluble in water by ferrous sulfate that ironic hydroxide adds the suspension that water stirs into, and adds ammoniacal liquor then to pH ≈ 7 precipitations, filters eccysis SO 4 2-After add water slurrying again and form.
Dechlorinating agent of the present invention has following characteristics:
1, degree of purification and chlorosity amount height, in inlet gas during HCl content 100-1000ppm, in the outlet purified gas HCl content less than 0.1ppm, this moment the chlorosity amount up to 40-50m%,
2, water resistance is good, and is unaffected less than 5% o'clock performance in the unstripped gas moisture content.
3, raw material is cheap and easy to get, and technology is simple.
Further specify the characteristics and the preparation of this dechlorinating agent below by embodiment.
Embodiment 1
Take by weighing the 46.8g ferrous sulfate, be dissolved in 100mlH 2Among the O, progressively drip 3.0mol/L ammoniacal liquor and stirring again, to pH ≈ 7.0, filtration washing is to there not being SO 4 2-, filter cake is added the suitable quantity of water making beating, make its dispersion, add then and contain 11gCaO, 39gNa 2CO 3, 12g γ-AlOOH and the bentonitic mixed powder of 32g, carry out mixed grind and become paste, paste is placed back extruded moulding more than 4 hours, in 80-120 ℃ of drying 2 hours, 300-400 ℃ of roasting promptly got dechlorinating agent A in 2 hours then.
Embodiment 2
Take by weighing the 46.8g ferrous sulfate, be dissolved in the 100ml water, progressively drip 3.0mol/L ammoniacal liquor again, be stirred to pH ≈ 7.0, filtration washing is to there not being SO 4 2-, filter cake added contains 2gNH 4HCO 3With 5ml colloid SiO 2The slurrying again of mixing solutions (20m%) makes Fe (OH) 3Disperse, add then and contain 11gCaO, 39gNa 2CO 3, 12g γ-AlOOH and the bentonitic mixed powder of 20g, carry out mixed grind and become paste, paste is placed extruded moulding after 5-6 hour, in 80-120 ℃ of drying 2 hours, 300-400 ℃ of roasting promptly got dechlorinating agent B in 2 hours then.
Embodiment 3
Take by weighing the 46.8g ferrous sulfate and make the ironic hydroxide slurry, sneak into 25gCaO, 30gNa again by embodiment 1 described method 2CO 3, 19g γ-AlOOH and 10g wilkinite, placed 6 hours after the mixed grind, in 80-120 ℃ of drying 2 hours, 300-400 ℃ of roasting promptly got dechlorinating agent C in 2 hours.
Embodiment 4
Take by weighing the 72.8g ferrous sulfate, make ferric hydroxide precipitate, add and contain 2g urea and 3ml colloid SiO by embodiment 1 or 2 2The water of mixing solutions (20m%) is made the ironic hydroxide slurry, sneaks into 38gCaO, 15gNa again 2CO 3, 9g γ-AlOOH and 10g wilkinite, place 5-6 hour extrusion after the mixed grind, in 80-120 ℃ of drying more than 2 hours, 300-400 ℃ of roasting be more than 2 hours, dechlorinating agent D.
Embodiment 5
Take by weighing the 39.8g ferrous sulfate, make the ironic hydroxide slurry, sneak into 17gCaO, 36gNa again by embodiment 1 described method 2CO 3, 16g γ-AlOOH and 15g wilkinite, fully place extruded moulding after 6-7 hour after the mixed grind, 80-120 ℃ of drying 2 hours, 300-400 ℃ of roasting 2 hours, dechlorinating agent E.
Embodiment 6
Present embodiment removes the test result of HCl performance for dechlorinating agent A-E.The dechlorinating agent strength test is measured on intelligent intensity meter, in pressure measurement intensity (or shatter strength).The dechlorination performance test is carried out in φ 10mm stainless steel reactor, and dechlorinating agent A-E is broken into 20-40 purpose small-particle, respectively gets 2.0ml and packs in the reactor, and gas is H 2-N 2Gas mixture, volume space velocity 1000-3000h -1, allocate HCl amount into and be 1000ppm, temperature of reaction 100-300 ℃, the pressure normal pressure, the chlorosity amount with HCl in the exit gas dechlorinating agent adsorptive capacity during greater than 0.1ppm represent, promptly penetrate chlorosity.
The alkali lye absorption is adopted in the measurement of hydrogenchloride, spectrophotometry, and sample was pulverized drying after chlorosity mensuration adopted and will penetrate, water logging after the weighing, cl content in the mensuration water calculates then, and the analysis of chlorine also is a spectrophotometry.Its result such as table 1.
Table 1
Dechlorinating agent Intensity N/cm Air speed h -1 Temperature of reaction ℃ Chlorosity m%
A B C D E 46 55 63 62 59 3000 3000 3000 3000 3000 1000 100 200 200 100 100 300 39.8 47.6 44.3 43.9 45.8 50.2

Claims (4)

1, a kind of dechlorinating agent is characterized in that containing CaO, Na 2CO 3Or NaHCO 3, Fe (OH) 3And the active constituent and the inorganic clay wilkinite carrier of γ-AlOOH formation, wherein the weight percentage of each component is respectively CaO 10-40%, Na by oxide compound 2O 10-23%, Al 2O 35-11%, Fe 2O 311-24%, inorganic bentonite 10-40%.
2, dechlorinating agent as claimed in claim 1 is characterized in that also containing colloid SiO 2, colloid SiO 20-5% for component weight percentage.
3, the preparation method of claim 1 or 2 described dechlorinating agents is characterized in that step is:
(1) ironic hydroxide is added water, perhaps also add the colloid SiO of proportional quantity 2The expanding agent NH of 0-5% with the batching overall weight percent 4HCO 3Or urea, stir into suspension:
(2) CaO, the Na of adding proportional quantity in (1) gained suspension 2CO 3Or NaHCO 3, γ-AlOOH and wilkinite, mixed grind becomes paste, then, places more than 4 hours;
(3) with behind the paste extruded moulding in 80-120 ℃ of drying more than 2 hours, again 300-400 ℃ of roasting more than 2 hours promptly.
4, preparation method as claimed in claim 3, it is soluble in water by ferrous sulfate to it is characterized in that ironic hydroxide adds the suspension that water stirs into, and adds ammoniacal liquor then to pH ≈ 7 precipitations, filters eccysis SO 4 2-After add water slurrying again and form.
CN98121676A 1998-11-24 1998-11-24 Dechlorinating agent and its preparing method Expired - Lifetime CN1095388C (en)

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Application Number Priority Date Filing Date Title
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CN1095388C true CN1095388C (en) 2002-12-04

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Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100354030C (en) * 2004-11-01 2007-12-12 中国科学院生态环境研究中心 Dechlorination agent and preparation method thereof
CN100453147C (en) * 2005-12-07 2009-01-21 西北化工研究院 Antichlor for catalytic reforming regenerated gas and preparation method
CN101804298B (en) * 2010-04-10 2013-03-27 太原理工大学 Method for preparing chlorine arresting agent
CN103127903B (en) * 2013-03-22 2014-12-17 沈阳三聚凯特催化剂有限公司 Normal-temperature dechlorinating agent
CN103316624B (en) * 2013-06-08 2015-03-04 华烁科技股份有限公司 Dephosphorization agent and preparation method thereof
CN109382388B (en) * 2017-08-07 2022-05-13 中国石化扬子石油化工有限公司 Method for preparing fresh dechlorinating agent from waste dechlorinating agent
CN115869900A (en) * 2022-12-27 2023-03-31 上海恒业微晶材料科技股份有限公司 Composite dechlorinating agent and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4639259A (en) * 1985-10-09 1987-01-27 Kaiser Aluminum & Chemical Corporation Promoted scavenger for purifying HCl-contaminated gases
US4762537A (en) * 1985-11-07 1988-08-09 Aluminum Company Of America Adsorbent for HCl comprising alumina and acid-treated Y zeolite
CN1064099A (en) * 1992-03-21 1992-09-02 南京化工学院 Dechlorinating agent
CN1147977A (en) * 1996-04-26 1997-04-23 湖北省化学研究所 Refined antichlor and method for preparing same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4639259A (en) * 1985-10-09 1987-01-27 Kaiser Aluminum & Chemical Corporation Promoted scavenger for purifying HCl-contaminated gases
US4762537A (en) * 1985-11-07 1988-08-09 Aluminum Company Of America Adsorbent for HCl comprising alumina and acid-treated Y zeolite
CN1064099A (en) * 1992-03-21 1992-09-02 南京化工学院 Dechlorinating agent
CN1147977A (en) * 1996-04-26 1997-04-23 湖北省化学研究所 Refined antichlor and method for preparing same

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Denomination of invention: High performance dechloridizing agent and preparation thereof

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