CN105233875B - A kind of preparation method of ultralow mercury catalyst for VCM synthesis - Google Patents

A kind of preparation method of ultralow mercury catalyst for VCM synthesis Download PDF

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CN105233875B
CN105233875B CN201510703909.8A CN201510703909A CN105233875B CN 105233875 B CN105233875 B CN 105233875B CN 201510703909 A CN201510703909 A CN 201510703909A CN 105233875 B CN105233875 B CN 105233875B
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chloride
mercury
phase adsorption
gas phase
ultralow
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CN105233875A (en
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李通
常炳恩
李建平
李玉强
李庆
孙玉梅
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Li Tong
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Ningxia Xinlong Lantian Technology Co Ltd
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06Halogens; Compounds thereof
    • B01J27/08Halides
    • B01J27/10Chlorides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/24Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0234Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
    • B01J31/0235Nitrogen containing compounds
    • B01J31/0239Quaternary ammonium compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • B01J31/28Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of the platinum group metals, iron group metals or copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0209Impregnation involving a reaction between the support and a fluid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/07Preparation of halogenated hydrocarbons by addition of hydrogen halides
    • C07C17/08Preparation of halogenated hydrocarbons by addition of hydrogen halides to unsaturated hydrocarbons

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Abstract

The present invention provides a kind of preparation method of ultralow mercury catalyst for VCM synthesis, includes preparation, the absorption of activated carbon, and the absorption includes Gas Phase Adsorption mercury chloride and liquid phase adsorption collaboration accelerator;Ultralow mercury catalyst prepared by the present invention, obtained ultralow mercury catalyst is by weight percentage, chloride containing mercury 0.93 1.0%, zinc chloride 2.4 2.5%, barium chloride 1.2 2.5%, tetrabutylammonium chloride 1.2 3.75%, the ammonia palladium 1.25 2.4% of dichloro four, water 0.2%, mechanical strength 96.6 96.9%, 3~6mm of granularity(97‑97.5%), the 505g/l of bulk density 500;Ultralow mercury catalyst prepared by the present invention, for vinyl chloride synthesis reaction, conversion of alkyne is up to 99.90 99.91%, and vinyl chloride selectivity is up to 99.9 100%, and the yield of vinyl chloride is up to 94.2 94.5%.

Description

A kind of preparation method of ultralow mercury catalyst for VCM synthesis
Technical field
The present invention relates to a kind of preparation method of the ultralow mercury catalyst for VCM synthesis, belong to fine chemistry technology Field.
Background technology
The polyvinyl chloride synthesized by VCM(PVC), it is the thermoplastic articles raw material of yield maximum in the world One of, it is widely used in the fields such as materials for construction, packaging material, electric equipment products, medical industry, coating and adhesive.
The industrialized production of current synthesis vinyl chloride thereof monomer in the world is based on ethylene process.Fluctuated by crude oil price larger Influence, occupies critical role at home by acetylene through hydrogen chloride production PVC.Acetylene hydrochlorination reaction industrial at present, mainly The high mercury catalyst that mercury chloride load capacity is 12% ~ 15% is used, its consumption to mercury accounts for the 60% of domestic mercury usage amount, and Health to environment and the mankind causes serious harm.
For the rare of mercury resource and the pollution to environment, and both at home and abroad to the increasingly severe of mercury pollution prevention and control policy, It is raw meeting industry in the urgent need to being had breakthrough in the improvement to mercury chloride performance and the research of high-performance environment protection type catalyst While production needs, mercury resource consumption and the pollution and harm to environment and human health is greatly lowered.
Existing low-mercury catalyst, has the following disadvantages:
(1)Mercury content is high;
(2)Service life is short;
(3)Catalytic performance is poor, for vinyl chloride synthesis reaction, and conversion of alkyne is less than 99.8%, the selection of vinyl chloride vinyl chloride Property and yield are low.
The content of the invention
There is provided a kind of ultralow mercury catalyst for VCM synthesis to solve the deficiency that prior art is present by the present invention Prepare and its mercury recovery method, to realize following goal of the invention:
(1)Ultralow mercury catalyst prepared by the present invention, the adsorbing chlorinated mercury in activated carbon center, obtained ultralow mercury catalysis Agent by weight percentage, chloride containing mercury 0.93-1.0%, zinc chloride 2.4-2.5%, barium chloride 1.2-2.5%, tetrabutylammonium chloride 1.2-3.75%, the ammonia palladium 1.25-2.4% of dichloro four, water 0.2%, mechanical strength 96.6-96.9%, 3~6mm of granularity(97-97.5%), Bulk density 500-505g/l.
(2)Ultralow mercury catalyst prepared by the present invention, catalyst long service life.
(3)Catalyst prepared by the present invention is used for vinyl chloride synthesis reaction, and conversion of alkyne reaches 99.90-99.91%, chloroethene Alkene selectively reaches 99.9-100%, and the yield of vinyl chloride reaches 94.2-94.5%.
To solve above technical problem, the present invention uses following technical scheme:
A kind of preparation method of ultralow mercury catalyst for VCM synthesis, includes preparation, the absorption of activated carbon, described Absorption includes Gas Phase Adsorption mercury chloride and liquid phase adsorption collaboration accelerator.
The following is the further improvement to above-mentioned technical proposal:
The Gas Phase Adsorption mercury chloride includes first stage Gas Phase Adsorption, the first stage Gas Phase Adsorption, control pressure For 0.6-0.7MPa, temperature is 540-560 DEG C, and mass space velocity is 7h-1, adsorb 15min.
The Gas Phase Adsorption mercury chloride includes second stage Gas Phase Adsorption, and the second stage Gas Phase Adsorption is depressurized to pressure Power is 0.4-0.5 MPa, and temperature is 420-440 DEG C, and mass space velocity is 8h-1, adsorb 10min.
The Gas Phase Adsorption mercury chloride includes phase III Gas Phase Adsorption, and the phase III Gas Phase Adsorption boosts to pressure Power is 0.7-0.8 MPa, and temperature is 560-570 DEG C, and mass space velocity is 6h-1, adsorb 5min.
The Gas Phase Adsorption mercury chloride, the content for controlling mercury chloride is 1.0-1.1%.
The liquid phase adsorption, including immersion absorption, the immersion absorption, soak 2 small under 120-125 DEG C of temperature conditionss When, dried under 110 DEG C of temperature conditionss to aqueous less than 0.2%.
The liquid phase adsorption, including vacuum infiltration absorption, vacuum infiltration absorption are vacuumized, reach -0.035 ~ - 30s is kept after 0.038MPa pressure, then is recovered to normal pressure, in soaking 5min under normal pressure.
Using above technical scheme, beneficial effects of the present invention are:
(1)Ultralow mercury catalyst prepared by the present invention, the adsorbing chlorinated mercury in activated carbon center, obtained ultralow mercury catalysis Agent by weight percentage, chloride containing mercury 0.93-1.0%, zinc chloride 2.4-2.5%, barium chloride 1.2-2.5%, tetrabutylammonium chloride 1.2-3.75%, the ammonia palladium 1.25-2.4% of dichloro four, water 0.2%, mechanical strength 96.6-96.9%, 3~6mm of granularity(97-97.5%), Bulk density 500-505g/l.
(2)Ultralow mercury catalyst prepared by the present invention, catalyst long service life, up to 8500 hours.
(3)Catalyst prepared by the present invention is used for vinyl chloride synthesis reaction, and conversion of alkyne is 99.90-99.91%, chloroethene Alkene is selectively 99.9-100%, and the yield of vinyl chloride is 94.2-94.5%.
Embodiment
The preferred embodiments of the present invention are illustrated below, it will be appreciated that preferred embodiment described herein is only used In the description and interpretation present invention, it is not intended to limit the present invention.
A kind of preparation method of the ultralow mercury catalyst for VCM synthesis of embodiment 1
The preparation of step 1, activated carbon
(1)The selection of feed coal
The feed coal is anthracite, and moisture is 6%, and content of ashes is 8.5%, and volatile matter content is 14.5%, fixed Carbon content is 71%.
(2)The deliming of feed coal
By smokeless coal grinding, 100 mesh sieves are crossed, coal dust are put into 30ppm polymeric aluminum chlorides solution, strong agitation, turned Speed is 5000r/min, after 2 minutes, and rotating speed is reduced to 500r/min, after stirring 10 minutes, filtering, and distillation is washed to during filtrate is in Property;Add in polyacrylamide solution, polyacrylamide concentration is 0.5ppm, and rotating speed is 400 r/min, after stirring 10 minutes, mistake Filter, it is in neutral that distillation, which is washed to filtrate, and content of ashes is 1.5% after deliming.
(3)Charing
By by the coal dust of deliming, in the case where N2 flows are 20ml/mim protection, carbonized, carbonization temperature initial temperature For 300 DEG C, with 2 DEG C/min heating rate, 400 DEG C are risen to, carbonizes 2.5 hours, obtains carbonized material.
(4)Once activate
By the coal dust acid dip after charing, described acid, including:60% phosphoric acid, tartaric acid, stearic acid, mass ratio For 3:1:2, acid is 3 with the mass ratio of fixed carbon in coal dust:1, soak 5 hours, wash, dry.
(5)Re-activation
In coal dust after once activating, the mixed liquor for being placed in re-activation agent, soak 2 hours, the re-activation Agent is zinc chloride, bismuth chloride, magnesium chloride, plumbi nitras, and mass ratio is 3:2:1:1, the mass ratio of re-activation agent and fixed carbon For 1:0.8, it is then 10ml/mim, at 480 DEG C in N2 flows, activates 2 hours.
(6)Post processing
Activated material to be come out of the stove and be cooled to room temperature after cooling, is put into immersion in the hydrochloric acid solution that weight/mass percentage composition is 4% 12 small When, distilled water flushing to neutrality, drying.
The activated carbon iodine number 1250mg/g of preparation, methylene blue value 135mg/g, mesoporous is up to 97.5%, and carbon tetrachloride is adsorbed Value is that 120%, moisture content 2%, ash 1.5%, fixed carbon content are 75%, mechanical strength 98%, bulk density 398g/L, specific surface area For 1950m2/ g, average pore size is 2.7-3.1nm.
The preparation of step 2, carrier
(1)Prepare hydrochloric acid solution
500 kilograms of the hydrochloric acid solution that mass fraction is 0.5% is prepared with high purity hydrochloric acid and desalted water, room temperature is standby;
(2)Handle activated carbon
100 kilograms of selected activated carbons are put into(1)Soaked in the hydrochloric acid solution of preparation 30 minutes, during which using circulation Pump makes hydrochloric acid solution constantly flow, and then takes out filtering or is filtered dry, is done under 200 DEG C of temperature conditionss with centrifuge drying dehydration Dry to aqueous less than 3%, carrier is made.
Step 3, the preparation for cooperateing with accelerator adsorption liquid
PH=3 15% hydrochloric acid solution is prepared with hydrochloric acid and desalted water, appropriate collaboration accelerator is added, collaboration accelerator Mass content is 10%, and collaboration accelerator includes:Zinc chloride, barium chloride, tetrabutylammonium chloride, the ammonia palladium of dichloro four, mass ratio For:2:1:1:2.
Step 4, absorption
(1)Gas Phase Adsorption mercury chloride
A, pre-treatment
Activated carbon by pretreatment is fitted into adsorbent bed, high-purity mercury chloride is subjected to heating and gasifying, the chlorine of gas phase Change mercury to enter in the adsorbent bed equipped with activated carbon, first with nitrogen purge system, the foreign gas such as discharge oxygen, carbon dioxide,
B, first stage Gas Phase Adsorption
Control pressure is 0.6MPa, and temperature is 540 DEG C, and mass space velocity is 7h-1, adsorbent bed upper end is equipped with condenser, condensation Liquid reenters adsorbent bed after being regasified and adsorbed, after absorption 15min;
C, second stage Gas Phase Adsorption
Step-down processing is carried out, pressure is 0.4MPa in adsorbent bed after step-down, temperature is 420 DEG C, and mass space velocity is 8h-1, inhale Attached 10min;
D, phase III Gas Phase Adsorption
It is 0.7MPa to carry out after boosting processing, boosting pressure in adsorbent bed again, and temperature is 560 DEG C, and mass space velocity is 6h-1, 5min is adsorbed, as a circulation, after the circulation is completed, the circulation is repeated, during which detects the mercury chloride of charcoal absorption Content, the content for controlling mercury chloride is 1.0%, stops absorption.
(2)Liquid phase adsorption cooperates with accelerator
A, immersion absorption
Absorbent charcoal carrier after Gas Phase Adsorption mercury chloride is put into the collaboration accelerator adsorption liquid that step 3 is prepared In, the mass ratio of absorbent charcoal carrier and adsorption liquid is 1:5, soaked under 120 DEG C of temperature conditionss 2 hours, during which using circulation Pump makes adsorbent solution constantly flow, and then takes out filtering or is filtered dry with centrifuge drying dehydration, baking oven is put into, in 110 DEG C of temperature Dried under the conditions of degree to aqueous less than 0.2%;
B, vacuum infiltration absorption
Then will by immersion absorption absorbent charcoal carrier be placed again into collaboration accelerator adsorption liquid in, absorbent charcoal carrier with The mass ratio of adsorption liquid is 1:4, place into stainless-steel vacuum tank, vacuumized with vavuum pump, reach and protected after -0.035MPa pressure 30s is held, then is recovered to normal pressure, 5min is soaked under normal pressure, filtering is then taken out or is filtered dry with centrifuge drying dehydration, put Enter baking oven, dried under 110 DEG C of temperature conditionss to aqueous less than 0.2%, ultralow mercury catalyst is made.
Ultralow mercury catalyst prepared by the present invention, the adsorbing chlorinated mercury in activated carbon center, obtained ultralow mercury catalyst By weight percentage, chloride containing mercury 0.93%, zinc chloride 2.4%, barium chloride 1.2%, tetrabutylammonium chloride 1.2%, the ammonia of dichloro four Palladium 2.4%, water 0.2%, mechanical strength 96.6%, 3~6mm of granularity(97%), bulk density 500g/l.
A kind of preparation method of the ultralow mercury catalyst for VCM synthesis of embodiment 2
Using the preparation method of embodiment 1, the parameter of change is as follows:
Step 3, the preparation for cooperateing with accelerator adsorption liquid
PH=2.5 16% hydrochloric acid solution is prepared with hydrochloric acid and desalted water, appropriate collaboration accelerator is added, cooperates with accelerator Mass content be 12%, collaboration accelerator include:Zinc chloride, barium chloride, tetrabutylammonium chloride, the ammonia palladium of dichloro four, mass ratio For:2:2:3:1.
Step 4, absorption
(1)Gas Phase Adsorption mercury chloride
A, pre-treatment
It will be fitted into by absorbent charcoal carrier in adsorbent bed, high-purity mercury chloride is subjected to heating and gasifying, the mercury chloride of gas phase Enter in the adsorbent bed equipped with activated carbon, first with nitrogen purge system, the foreign gas such as discharge oxygen, carbon dioxide;
B, first stage Gas Phase Adsorption
Then control pressure is 0.7MPa, and temperature is 560 DEG C, and mass space velocity is 7h-1, adsorbent bed upper end be equipped with condenser, Condensate liquid reenters adsorbent bed after being regasified and adsorbed, and adsorbs 15min;
C, second stage Gas Phase Adsorption
Step-down processing is carried out, pressure is 0.5 MPa in adsorbent bed after step-down, temperature is 440 DEG C, and mass space velocity is 8h-1, inhale Attached 10min;
D, phase III Gas Phase Adsorption
It is 0.8 MPa to carry out after boosting processing, boosting pressure in adsorbent bed again, and temperature is 570 DEG C, and mass space velocity is 6h-1, 5min is adsorbed, as a circulation, after the circulation is completed, the circulation is repeated, during which detects the mercury chloride of charcoal absorption Content, the content for controlling mercury chloride is 1.1%.
(2)Liquid phase adsorption cooperates with accelerator
A, immersion absorption
Absorbent charcoal carrier after Gas Phase Adsorption mercury chloride is put into the collaboration accelerator adsorption liquid that step 3 is prepared In, the mass ratio of absorbent charcoal carrier and adsorption liquid is 1:5, soaked under 125 DEG C of temperature conditionss 2 hours, during which using circulation Pump makes adsorbent solution constantly flow, and then takes out filtering or is filtered dry with centrifuge drying dehydration, baking oven is put into, in 110 DEG C of temperature Dried under the conditions of degree to aqueous less than 0.2%;
B, vacuum infiltration absorption
Then it will be placed again into by the absorbent charcoal carrier for soaking absorption in the collaboration accelerator adsorption liquid that step 3 is prepared, The mass ratio of absorbent charcoal carrier and adsorption liquid is 1:5, place into stainless-steel vacuum tank, vacuumized with vavuum pump, reach- 30s is kept after 0.038MPa pressure, then is recovered to normal pressure, 5min is soaked under normal pressure, filtering is then taken out or uses centrifuge Drying dehydration is filtered dry, and is put into baking oven, is dried under 110 DEG C of temperature conditionss to aqueous less than 0.2%, and ultralow mercury catalyst is made.
Ultralow mercury catalyst prepared by the present invention, the adsorbing chlorinated mercury in activated carbon center, obtained ultralow mercury catalyst By weight percentage, chloride containing mercury 1.0%, zinc chloride 2.5%, barium chloride 2.5%, tetrabutylammonium chloride 3.75%, the ammonia of dichloro four Palladium 1.25%, water 0.2%, mechanical strength 96.9%, 3~6mm of granularity(97.5%), bulk density 505g/l.
The above-mentioned catalyst of embodiment 3 is used for vinyl chloride synthesis reaction
(1)Loading catalyst catalyst
Check that reactor is inside and outside without leak source before loading catalyst catalyst, tubulation inwall is clean, dry, no-sundries;Will Catalyst of the present invention is encased in each tubulation of reactor immediately after opening packaging, and loading catalyst will be completed in 0.5h, sincerely Moisture proof.
(2)Preheating
It is passed through 90~100 DEG C of drying HCl, 7~8m of speed control3/ h, continuous 8~10h, during which every 2h by reactor Put acid once in bottom.
(3)Synthesis vinyl chloride thereof is reacted
The molar ratio of acetylene, hydrogen chloride is controlled 1:1.1~1:1.3(100% purity), preheated temperature is up to 90 DEG C Mixed gas above is passed through reactor, and culture period 1 month adjusts acetylene gas intake, control according to reactor cooling capacity Temperature processed is between 110~125 DEG C;After culture period terminates, acetylene gas intake is adjusted according to reactor cooling capacity(30~ 50h-1), by reaction temperature control at 130 DEG C.
Catalyst of the present invention is used for vinyl chloride synthesis reaction, and conversion of alkyne reaches 99.90-99.91%, vinyl chloride selectivity Up to 99.9-100%, the yield of vinyl chloride reaches 94.2-94.5%, catalyst long service life, up to 8500 hours.
" mass space velocity " of the present invention, is defined as:The mass flow of mercury chloride(㎏·h-1)The quality of/activated carbon (kg).
Unless otherwise indicated, the percentage employed in the present invention is percetage by weight, ratio of the present invention, For mass ratio.
The general principle and principal character and advantages of the present invention of the present invention has been shown and described above.The skill of the industry Art personnel are it should be appreciated that the present invention is not limited to the above embodiments, and described in above-described embodiment and specification is explanation The principle of the present invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these Changes and improvements all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appending claims and Its equivalent thereof.

Claims (4)

1. a kind of preparation method of ultralow mercury catalyst for VCM synthesis, it is characterised in that:Preparation including activated carbon, Absorption, the absorption includes Gas Phase Adsorption mercury chloride and liquid phase adsorption collaboration accelerator;
The ultralow mercury catalyst, the adsorbing chlorinated mercury in activated carbon center, obtained ultralow mercury catalyst is with percentage by weight Meter, chloride containing mercury 0.93-1.0%, zinc chloride 2.4-2.5%, barium chloride 1.2-2.5%, tetrabutylammonium chloride 1.2-3.75%, dichloro Four ammonia palladium 1.25-2.4%, water 0.2%;
The Gas Phase Adsorption mercury chloride includes first stage Gas Phase Adsorption, the first stage Gas Phase Adsorption, and control pressure is 0.6-0.7MPa, temperature is 540-560 DEG C, and mass space velocity is 7h-1, adsorb 15min;
The Gas Phase Adsorption mercury chloride include second stage Gas Phase Adsorption, the second stage Gas Phase Adsorption, being depressurized to pressure is 0.4-0.5 MPa, temperature is 420-440 DEG C, and mass space velocity is 8h-1, adsorb 10min;
The Gas Phase Adsorption mercury chloride include phase III Gas Phase Adsorption, the phase III Gas Phase Adsorption, boosting to pressure is 0.7-0.8 MPa, temperature is 560-570 DEG C, and mass space velocity is 6h-1, adsorb 5min.
2. a kind of preparation method of ultralow mercury catalyst for VCM synthesis according to claim 1, its feature exists In the Gas Phase Adsorption mercury chloride, the content for controlling mercury chloride is 1.0-1.1%.
3. a kind of preparation method of ultralow mercury catalyst for VCM synthesis according to claim 1, its feature exists In, the liquid phase adsorption, including immersion absorption, the immersion absorption, soaked 2 hours under 120-125 DEG C of temperature conditionss, Dried under 110 DEG C of temperature conditionss to aqueous less than 0.2%.
4. a kind of preparation method of ultralow mercury catalyst for VCM synthesis according to claim 1, its feature exists In, the liquid phase adsorption, including vacuum infiltration absorption, the vacuum infiltration absorption, vacuumize, reach -0.035 ~ -0.038MPa 30s is kept after pressure, then is recovered to normal pressure, in soaking 5min under normal pressure.
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CN201710442649.2A CN107376998B (en) 2015-10-27 2015-10-27 Preparation method of ultralow-mercury catalyst for catalyzing acetylene and hydrogen chloride to synthesize vinyl chloride
CN201510703909.8A CN105233875B (en) 2015-10-27 2015-10-27 A kind of preparation method of ultralow mercury catalyst for VCM synthesis
CN201710443693.5A CN107321389B (en) 2015-10-27 2015-10-27 Preparation method of ultralow-mercury catalyst for catalytic synthesis of chloroethylene

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CN108043467B (en) * 2017-11-27 2020-10-02 宁夏新龙蓝天科技股份有限公司 Mercury-free catalyst for improving yield of chloroethylene and preparation method thereof
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