CN107376861A - A kind of preparation method of recyclability deoxidier - Google Patents

A kind of preparation method of recyclability deoxidier Download PDF

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Publication number
CN107376861A
CN107376861A CN201710763980.4A CN201710763980A CN107376861A CN 107376861 A CN107376861 A CN 107376861A CN 201710763980 A CN201710763980 A CN 201710763980A CN 107376861 A CN107376861 A CN 107376861A
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deoxidier
recyclability
mixture
preparation
iron powder
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杨立军
黄婷
林大伟
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Changzhou Ruitan Trading Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/041Oxides or hydroxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/14Diatomaceous earth
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/10Single element gases other than halogens
    • B01D2257/104Oxygen

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Cosmetics (AREA)

Abstract

The invention discloses a kind of preparation method of recyclability deoxidier, belong to deoxidier technical field.The present invention is using iron powder as base-material, diatomite and activated carbon are carrier, first iron oxide is reduced, reduced iron powder and diatomite, salt and Grape Skin blending are fermented, reduced iron powder, salt and diatom generation free state mixture, the oxygen uptake performance of metallic element is set to improve the deoxidation effect of activated carbon using microorganism.Liquid feeding body whipping cream, compatibility is improved, continuously adds alkaline earth oxide, improve the content of reduced iron powder, then its internal void space is become big with montmorillonite, improve its deoxidation capacity.Finally, liquefied mixture with deoxygenation function is coated in carrier surface, deoxidier is made, the use of deoxidier, outermost layer saturation come off, and expose new deoxidation composition, extend deoxidier regeneration cycle, reduce energy expenditure, significantly improve the regenerability and deoxidation capacity of deoxidier, have broad application prospects.

Description

A kind of preparation method of recyclability deoxidier
Technical field belongs to deoxidier technical field the invention discloses a kind of preparation method of recyclability deoxidier. Background technology
The research of domestic deoxidier starts from 20th century the fifties end, and it is that deoxidation is urged that Nan Hua companies, which start production 0603 the sixties, Agent.0603 system is using the oxide of copper as key component, and it both can be in H2In the presence of deoxidation, can also be under hydrogen-free condition Deoxidation, deoxidation depth are 1.0 × 10-5, deoxidizing capacity 10ml/g.0605 after improvement improves deoxy activity and machinery Intensity, depth are 5.0 × 10-6.The said firm in 1984 releases BH series dehydrogenation catalysts again, and BH series is using Ni as activearm Point, can both there is H2Under conditions of deoxidation, chemical absorbing deoxidation can also be made, can be by general nitrogen, argon gas and hydro carbons mixing qi exhaustion To 5.0 × 10-6, deoxidizing capacity is up to 25ml/g.
The DO series deoxidiers that the Lanzhou Chemistry and Physics Institute of the Chinese Academy of Sciences develops are using Pt, Pa as active component, for synthetic gas deoxidizing. Because its preparation method is to use infusion process, thin-shell type bimetallic or single-metal reforming catalyst is made, so efficiency is higher, deoxy activity Height, stability is good, and side reaction is few;It is but undesirable when CO is high in raw material.The Dalian Chemistry and Physics Institute of the Chinese Academy of Sciences develops a kind of palladium/manganese oxide Deoxidier, its principle are that the oxide of low price manganese has high activity to micro amount of oxygen, can react generation value Mn at normal temperatures With reaching deoxidation mesh, the oxide hydrogen reduction of value Mn has recovered deoxy activity, led to oxide again into the oxide of low price manganese Cross deoxidation and regeneration, remove the water of generation, so as to reach deoxidier it is long-term, stably, efficient deoxy performance.
With industrial expansion, the requirement to high-purity gas improves constantly from quality and quantity, the requirement to deoxidier Also accordingly increasing, especially recyclability deoxidier.So the new renewable deoxidier of exploitation is by before with wide market Scape.
The content of the invention
The technical problems to be solved by the invention:Have that regeneration rate is relatively low low with deoxidation capacity to be lacked for current deoxidier Fall into, there is provided a kind of preparation method of recyclability deoxidier.
In order to solve the above-mentioned technical problem, the present invention is using technical scheme as described below:
A kind of preparation method of recyclability deoxidier, it is characterised in that specifically preparation process is:
(1)80~100g steels are weighed, after grating into strips, strip-like-shaped steel is obtained, strip-like-shaped steel is put into roaster Aoxidized, iron oxide is obtained after oxidation, continue iron oxide being put into roaster, the reduction reaction under nitrogen guard mode, Reduced iron powder is obtained after reduction;
(2)The grinding of 4~6g diatomite is weighed again, and diatomite powder is obtained after grinding;
(3)Reduced iron powder, salt and diatomite powder are mixed, mixture is obtained after stirring, continues to add into mixture Enter the Grape Skin of mixture quality 0.6%, be fitted into fermentation tank, be sealed by fermentation, after fermentation ends, take out tunning, as swim Amorph mixture;
(4)Added again into free state mixture 3~5g activated carbons, 100~200mL fresh liquid milks oil, 2~4g calcium oxide and 800~1000mL water is mixed, and liquefied mixture is obtained after stirring;
(5)Take montmorillonite to be taken out after being soaked in water, freeze 3~5min with liquid nitrogen spraying immediately, after its clear-cutting forestland room temperature, obtain To pretreatment montmorillonite;By liquefied mixture with hairbrush coated in montmorillonite surface is pre-processed, it is 2~5mm to control coating thickness, After coating terminates, deoxidier base substrate is obtained;
(6)Deoxidier base substrate is put into baking oven, is transferred in Muffle furnace after being dried at 105~110 DEG C, is burnt at 300~400 DEG C Knot, produces recyclability deoxidier after discharging.
Step(1)The oxidizing temperature of described roaster is 950~1000 DEG C, and the reduction temperature of roaster is 800~900 DEG C, oxidization time is 2~3h, and the recovery time is 1~2h.
Step(2)Described milling time is 6~9min.
Step(3)The mass ratio of described reduced iron powder, salt and diatomite powder is 5:1:2, mixing time be 7~ 9min, fermentation temperature are 45~55 DEG C, and fermentation time is 7~9 days.
Step(4)Described mixing time is 10~30min.
Step(5)Described soak time is 1~2h.
Step(6)Described drying time is 1~2h, and sintering time is 1~2h.
The beneficial effects of the invention are as follows:
For the present invention using iron powder as base-material, diatomite and activated carbon are carrier, and iron oxide is reduced first, gone back after reduction Former iron powder, reduced iron powder are easy to aoxidize, and reduced iron powder and diatomite, salt and Grape Skin blending are fermented, utilize microorganism pair Reduced iron powder, salt and diatomite act and generate free state mixture, will be free under the self-crosslinking of microorganism State mixture is incorporated into activated carbon surface, improves the deoxidation effect of activated carbon using the oxygen uptake performance of metallic element so that final Obtained deoxidier has splendid oxygen uptake performance, adds fresh liquid milk oil, improves free state mixture and activated carbon Compatibility, alkaline earth oxide is continuously added, considerably improve the content of active constituent reduced iron powder in deoxidier, then with Montmorillonite splits principle using ice, deoxidier carrier inside interstitial space can be made to become big, taken off so as to improve it as deoxidation agent carrier Oxygen capacity, finally, the liquefied mixture with deoxygenation function is coated in carrier surface, deoxidier is made, with deoxidier Use, the deoxidation capacity that its outermost layer has the liquefied mixture of deoxygenation function can progressively reach saturation state and natural aging takes off Fall, expose internal new deoxygenation function composition again, so as to reach regeneration purpose, extend deoxidier regeneration cycle, subtract Energy expenditure is lacked, has significantly improved the regenerability and deoxidation capacity of deoxidier, have broad application prospects.
Embodiment
80~100g steels are weighed, after grating into strips, obtain strip-like-shaped steel, strip-like-shaped steel is put into temperature is 2~3h of oxidation is carried out in 950~1000 DEG C of roaster, iron oxide is obtained after oxidation, continues iron oxide being put into roaster, It is 800~900 DEG C to set temperature, 1~2h of reduction reaction under nitrogen guard mode, reduced iron powder is obtained after reduction, then weigh 4 ~6g diatomite grinds 6~9min, and diatomite powder is obtained after grinding, is in mass ratio 5:1:2 by reduced iron powder, salt and silicon Diatomaceous earth powder mixes 7~9min, and mixture is obtained after stirring, continues to add mixture quality 0.6 into mixture
% Grape Skin, is fitted into fermentation tank, is sealed by fermentation 7~9 days under conditions of being 45~55 DEG C in temperature, after fermentation ends, Tunning, as free state mixture are taken out, then 3~5g activated carbons, 100~200mL liquid are added into free state mixture Body whipping cream, 2~4g calcium oxide and 800~1000mL water mix 10~30min, and liquefied mixture is obtained after stirring;Take Montmorillonite is soaked in water after 1~2h and taken out, and freezes 3~5min with liquid nitrogen spraying immediately, after its clear-cutting forestland room temperature, obtains pre- Montmorillonite is handled, by liquefied mixture with hairbrush coated in pretreatment montmorillonite surface, it is 2~5mm to control coating thickness, coating After end, deoxidier base substrate is obtained, deoxidier base substrate is put into baking oven, Muffle is transferred to after drying 1~2h at 105~110 DEG C In stove, 1~2h is sintered at 300~400 DEG C, recyclability deoxidier is produced after discharging.
Example 1 weighs 80g steels, after grating into strips, obtains strip-like-shaped steel, and strip-like-shaped steel is put into temperature is Oxidation 2h is carried out in 950 DEG C of roaster, iron oxide is obtained after oxidation, continues iron oxide being put into roaster, temperature is set For 800 DEG C, the reduction reaction 1h under nitrogen guard mode, reduced iron powder is obtained after reduction, then weighs 4g diatomite grinding 6min, Diatomite powder is obtained after grinding, is in mass ratio 5:1:Reduced iron powder, salt and diatomite powder are mixed 7min by 2, Mixture is obtained after stirring, continues to add the Grape Skin of mixture quality 0.6% into mixture, is fitted into fermentation tank, in temperature To be sealed by fermentation 7 days under conditions of 45 DEG C, after fermentation ends, tunning, as free state mixture are taken out, then to free state 3g activated carbons, 100mL fresh liquid milks oil, 2g calcium oxide and 800mL water are added in mixture and mixes 10min, after stirring To liquefied mixture;Take montmorillonite to be soaked in water after 1h to take out, freeze 3min with liquid nitrogen spraying immediately, treat its clear-cutting forestland room temperature Afterwards, obtain pre-processing montmorillonite, by liquefied mixture with hairbrush coated in pretreatment montmorillonite surface, control the coating thickness to be 2mm, after coating terminates, deoxidier base substrate is obtained, deoxidier base substrate is put into baking oven, Muffle is transferred to after drying 1h at 105 DEG C In stove, 1h is sintered at 300 DEG C, recyclability deoxidier is produced after discharging.
Example 2
90g steels are weighed, after grating into strips, obtain strip-like-shaped steel, strip-like-shaped steel is put into the roasting that temperature is 950 DEG C Oxidation 2h is carried out in stove, iron oxide is obtained after oxidation, continues iron oxide being put into roaster, it is 850 DEG C to set temperature, in nitrogen Reduction reaction 1h under gas shielded state, obtains reduced iron powder after reduction, then weighs 5g diatomite grinding 8min, and silicon is obtained after grinding Diatomaceous earth powder, it is in mass ratio 5:1:Reduced iron powder, salt and diatomite powder are mixed 8min by 2, are mixed after stirring Compound, continue to add the Grape Skin of mixture quality 0.6% into mixture, be fitted into fermentation tank, in the condition that temperature is 50 DEG C It is lower to be sealed by fermentation 8 days, after fermentation ends, take out tunning, as free state mixture, then added into free state mixture 4g activated carbons, 150mL fresh liquid milks oil, 3g calcium oxide and 900mL water mix 20min, and liquefied mixture is obtained after stirring; Take montmorillonite to be soaked in water after 1h to take out, freeze 4min with liquid nitrogen spraying immediately, after its clear-cutting forestland room temperature, pre-processed Montmorillonite, by liquefied mixture with hairbrush coated in montmorillonite surface is pre-processed, it is 4mm to control coating thickness, after coating terminates, Deoxidier base substrate is obtained, deoxidier base substrate is put into baking oven, is transferred in Muffle furnace after drying 1h at 105 DEG C, is burnt at 350 DEG C 1h is tied, recyclability deoxidier is produced after discharging.
Example 3
100g steels are weighed, after grating into strips, obtain strip-like-shaped steel, strip-like-shaped steel is put into the roasting that temperature is 1000 DEG C Burn in stove and carry out oxidation 3h, obtain iron oxide after oxidation, continue iron oxide being put into roaster, it is 900 DEG C to set temperature, Reduction reaction 2h under nitrogen guard mode, obtains reduced iron powder after reduction, then weighs 6g diatomite grinding 9min, is obtained after grinding Diatomite powder, it is in mass ratio 5:1:Reduced iron powder, salt and diatomite powder are mixed 9min by 2, are obtained after stirring Mixture, continue to add the Grape Skin of mixture quality 0.6% into mixture, be fitted into fermentation tank, in the bar that temperature is 55 DEG C It is sealed by fermentation 9 days under part, after fermentation ends, takes out tunning, as free state mixture, then add into free state mixture Enter 5g activated carbons, 200mL fresh liquid milks oil, 4g calcium oxide and 1000mL water and mix 30min, liquid mixing is obtained after stirring Thing;Take montmorillonite to be soaked in water after 2h to take out, freeze 5min with liquid nitrogen spraying immediately, after its clear-cutting forestland room temperature, obtain pre- Montmorillonite is handled, by liquefied mixture with hairbrush coated in pretreatment montmorillonite surface, it is 5mm to control coating thickness, coating knot Shu Hou, deoxidier base substrate is obtained, deoxidier base substrate is put into baking oven, be transferred to after drying 2h at 110 DEG C in Muffle furnace, 400 2h is sintered at DEG C, recyclability deoxidier is produced after discharging.
The deoxidier that comparative example is produced with Guangzhou company takes off to recyclability produced by the present invention as a comparison case Deoxidier in oxygen agent and comparative example is detected, and testing result is as shown in table 1:1st, method of testing
Deoxidation depth test is detected by the standard with deoxidation deep regenerative time experiment, and deoxidation depth is oxygen after gas deoxidation The ratio of oxygen volume before volume and gas deoxidation;
And the deoxidation capacity of product is detected, deoxidation capacity refers to that unit mass deoxidier is capable of the oxygen volume of adsorbing and removing, tool Body testing result is as shown in table 1:
Table 1
It can be seen from data in table 1, the deoxidizing capacity of recyclability deoxidier produced by the present invention is strong, and deoxidation capacity is high, and energy It is enough voluntarily to regenerate, there is wide prospect of the application.

Claims (7)

1. a kind of preparation method of recyclability deoxidier, it is characterised in that specifically preparation process is:
(1)80~100g steels are weighed, after grating into strips, strip-like-shaped steel is obtained, strip-like-shaped steel is put into roaster Aoxidized, iron oxide is obtained after oxidation, continue iron oxide being put into roaster, the reduction reaction under nitrogen guard mode, Reduced iron powder is obtained after reduction;
(2)The grinding of 4~6g diatomite is weighed again, and diatomite powder is obtained after grinding;
(3)Reduced iron powder, salt and diatomite powder are mixed, mixture is obtained after stirring, continues to add into mixture Enter the Grape Skin of mixture quality 0.6%, be fitted into fermentation tank, be sealed by fermentation, after fermentation ends, take out tunning, as swim Amorph mixture;
(4)Added again into free state mixture 3~5g activated carbons, 100~200mL fresh liquid milks oil, 2~4g calcium oxide and 800~1000mL water is mixed, and liquefied mixture is obtained after stirring;
(5)Take montmorillonite to be taken out after being soaked in water, freeze 3~5min with liquid nitrogen spraying immediately, after its clear-cutting forestland room temperature, obtain To pretreatment montmorillonite, by liquefied mixture with hairbrush coated in montmorillonite surface is pre-processed, it is 2~5mm to control coating thickness, After coating terminates, deoxidier base substrate is obtained;
(6)Deoxidier base substrate is put into baking oven, is transferred in Muffle furnace after being dried at 105~110 DEG C, is burnt at 300~400 DEG C Knot, produces recyclability deoxidier after discharging.
A kind of 2. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(1)It is described The oxidizing temperature of roaster be 950~1000 DEG C, the reduction temperature of roaster is 800~900 DEG C, and oxidization time is 2~3h, Recovery time is 1~2h.
A kind of 3. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(2)It is described Milling time be 6~9min.
A kind of 4. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(3)It is described Reduced iron powder, the mass ratio of salt and diatomite powder be 5:1:2, mixing time is 7~9min, fermentation temperature is 45~ 55 DEG C, fermentation time is 7~9 days.
A kind of 5. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(4)It is described Mixing time be 10~30min.
A kind of 6. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(5)It is described Soak time be 1~2h.
A kind of 7. preparation method of recyclability deoxidier according to claim 1, it is characterised in that:Step(6)It is described Drying time be 1~2h, sintering time is 1~2h.
CN201710763980.4A 2017-08-30 2017-08-30 A kind of preparation method of recyclability deoxidier Withdrawn CN107376861A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109294338A (en) * 2018-08-31 2019-02-01 王成 A kind of preparation method of metal protection deoxidier
CN111792926A (en) * 2020-07-23 2020-10-20 李笑天 Method for preparing embryo body by using rare earth element-iron oxide

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103653185A (en) * 2013-11-13 2014-03-26 广西弘耀祥科技有限公司 Moisture-proof deoxidizing agent for foodstuff
CN105076389A (en) * 2015-07-23 2015-11-25 小嵩保鲜技术(常熟)有限公司 Deoxidizer and making method thereof
CN105995383A (en) * 2016-06-16 2016-10-12 常熟市屹浩食品包装材料科技有限公司 Rapid deoxidizer for foods and preparation method of deoxidizer
CN106977230A (en) * 2017-05-14 2017-07-25 石磊 A kind of preparation method of water conservation self-repair type curing compound

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103653185A (en) * 2013-11-13 2014-03-26 广西弘耀祥科技有限公司 Moisture-proof deoxidizing agent for foodstuff
CN105076389A (en) * 2015-07-23 2015-11-25 小嵩保鲜技术(常熟)有限公司 Deoxidizer and making method thereof
CN105995383A (en) * 2016-06-16 2016-10-12 常熟市屹浩食品包装材料科技有限公司 Rapid deoxidizer for foods and preparation method of deoxidizer
CN106977230A (en) * 2017-05-14 2017-07-25 石磊 A kind of preparation method of water conservation self-repair type curing compound

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109294338A (en) * 2018-08-31 2019-02-01 王成 A kind of preparation method of metal protection deoxidier
CN109294338B (en) * 2018-08-31 2021-01-19 上海集优张力控制螺栓有限公司 Preparation method of metal protection deoxidizer
CN111792926A (en) * 2020-07-23 2020-10-20 李笑天 Method for preparing embryo body by using rare earth element-iron oxide
CN111792926B (en) * 2020-07-23 2023-12-19 李笑天 Method for preparing embryo body from rare earth element-iron oxide

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