WO1993012639A2 - Procede d'obtention d'un sorbant - Google Patents
Procede d'obtention d'un sorbant Download PDFInfo
- Publication number
- WO1993012639A2 WO1993012639A2 PCT/UA1992/000001 UA9200001W WO9312639A2 WO 1993012639 A2 WO1993012639 A2 WO 1993012639A2 UA 9200001 W UA9200001 W UA 9200001W WO 9312639 A2 WO9312639 A2 WO 9312639A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fact
- paragraphs
- paragraph
- celsius
- πρi
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/342—Preparation characterised by non-gaseous activating agents
- C01B32/348—Metallic compounds
Definitions
- the invention relates to a physically-chemical method of obtaining sorbents, and the nominal sorbents, the active start of the products, are carbon.
- a larger version of the product is not available for use in the case of accidents resulting from a loss of property or service.
- the invention is also related to the process of activating coal, which is obtained from industrial use of coal from waste.
- the purpose of the present invention is to generate a method for producing a component from a quick-disconnect or quick disconnect circuit.
- Another objective of the present invention is the creation of a method of obtaining a sorbent from a skewer for processing or treatment using biologic agents.
- ⁇ sche ⁇ dn ⁇ y purpose nas ⁇ yascheg ⁇ iz ⁇ b ⁇ e ⁇ eniya yavlyae ⁇ sya s ⁇ zdanie s ⁇ s ⁇ ba ⁇ lucheniya s ⁇ ben ⁇ a of s ⁇ lu ⁇ y ⁇ u ⁇ vy ⁇ ⁇ s ⁇ che ⁇ or ⁇ e ⁇ v with is ⁇ lz ⁇ vaniem ⁇ ezhima ⁇ a ⁇ b ⁇ nizatsii, ⁇ bes ⁇ echivayuscheg ⁇ ⁇ vyshenie vy ⁇ da tselev ⁇ g ⁇ ⁇ du ⁇ a with ⁇ shimi s ⁇ btsi ⁇ nnymi ⁇ a ⁇ a ⁇ e ⁇ is ⁇ i ⁇ ami.
- the goal set is achieved when _ ⁇ _ ne ⁇ e ⁇ yvny ⁇ dem ⁇ em ⁇ e ⁇ a ⁇ u ⁇ y ⁇ i ⁇ a ⁇ b ⁇ nizaiii in s ⁇ ede ⁇ i ⁇ - gaz ⁇ v ⁇ v ⁇ dya ⁇ in in ⁇ e ⁇ vale ⁇ 300 600 d ⁇ g ⁇ adus ⁇ v celsius ⁇ imaln ⁇ ⁇ echenie in 30 - 40 minutes the, im ⁇ egni ⁇ vanie s ⁇ lu ⁇ y ⁇ susches ⁇ vlyayu ⁇ d ⁇ s ⁇ de ⁇ zhaniya ⁇ l ⁇ ida na ⁇ iya in ⁇ b ⁇ aba ⁇ yvaem ⁇ y weight ⁇ 0.05 1.25 d ⁇ mass ⁇ vy ⁇ Percentages, and the subsequent activation of the economy are carried out by water at a temperature of 830 - 850 Celsius.
- ⁇ b ⁇ ab ⁇ a is ⁇ dn ⁇ y s ⁇ lu ⁇ y ⁇ u ⁇ vy ⁇ ⁇ s ⁇ che ⁇ or ⁇ e- ⁇ v or i ⁇ mixture s ⁇ de ⁇ zhaschey ⁇ me v ⁇ d ⁇ ne ⁇ as ⁇ v ⁇ imy ⁇ ⁇ e ⁇ in ⁇ vy ⁇ vesches ⁇ v (tsellyul ⁇ zy, gemitsellyul ⁇ zy, lignin and d ⁇ ugi ⁇ ), 14 - 17 ⁇ tsen ⁇ v v ⁇ d ⁇ as ⁇ v ⁇ imy ⁇ ⁇ e ⁇ in ⁇ vy ⁇ vesches ⁇ v, ⁇ as ⁇ v ⁇ m ⁇ l ⁇ is ⁇ g ⁇ na ⁇ iya ⁇ ed ⁇ lagae ⁇ , ⁇ a ⁇ ⁇ mnimum two ⁇ l ⁇ zhi ⁇ el- ny ⁇ moment.
- b ⁇ lshaya ⁇ e ⁇ ya mass is ⁇ dn ⁇ g ⁇ ⁇ lime ⁇ a; za ⁇ em, ⁇ i 450 - 600 g ⁇ adusa ⁇ celsius nachinayu ⁇ ⁇ e ⁇ blada ⁇ ⁇ tsessy ⁇ e- ⁇ mbinatsii and ⁇ li ⁇ ndensatsii, ⁇ mi ⁇ vaniya ugle ⁇ dny ⁇ ⁇ e ⁇ - me ⁇ ny ⁇ s ⁇ u ⁇ u ⁇ , ide ⁇ ⁇ s ⁇ e ⁇ enn ⁇ e ⁇ b ⁇ gaschenie ⁇ s ⁇ v ⁇ g ⁇ ⁇ s ⁇ a ⁇ - ⁇ a ugle ⁇ d ⁇ m.
- the best variant of the invention is that it was found that the best way is to optimize the cost of the unit at a cost of 1.2%. With a lower content of the emitted coals, the structure is reduced in the structure, the performance is worse, and the higher is the result of an increase in profit.
- the experimental data presented in table 1 below are clearly illustrative (example 4 with a salt content more - 5 - 1.25 weight percent and example 5 with a content of less than 0.05 weight percent compared to examples 1, 2 and 3).
- the processing unit is equipped with a quick part (for 10 kg in each * ,., Az.) It is processed in accordance with the principle ⁇ 1, with it only . ' • • By the party, that the trade union prudeblyuyut a separate krupulupu to k ⁇ .
- Expense of the content of salt is 0.06; 1.25; 1.40; 0.03 (examples 2–5) and 0.55 (examples 6–3) are mass percentages, and the combination of the imprisoned leads leads to 35 (examples 2 and 4), 30 (5) ), 20 ( ⁇ Sodium Jr ⁇ 7 7) and 55 minutes ( ⁇ Consequently opponent ⁇ 8 8).
- the finished product is free of charge, but on every 10th, it is processed at a cost of only 1.
- western societies (example 11), and the karabenization is carried out, respectively, in the temperature range 250 - 600 - 3 - Celsius for 40 minutes, at a temperature of 400 to 700 Celsius for 30 minutes and at a temperature of 300 to 700 Celsius for 40 minutes.
- P ⁇ ime ⁇ y 12 and 13 ⁇ z ⁇ i ⁇ ⁇ ime ⁇ a ⁇ data ⁇ ⁇ y ⁇ ⁇ ivedeny in ⁇ ablitse 2 is ⁇ dnuyu d ⁇ blenuyu s ⁇ lu ⁇ u ⁇ u ⁇ v ⁇ y ⁇ s ⁇ ch ⁇ i, ⁇ 10 ⁇ g ⁇ azh- dy ⁇ b ⁇ azets, It is processed in accordance with Example 2 with the difference. that, in case of example 12, the military unit is in a foreign environment in the nitrogen atmosphere), and in case of 13, it is in the air.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
- Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
Abstract
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU5019710/26 | 1991-12-26 | ||
SU915019710A RU2013120C1 (ru) | 1991-12-26 | 1991-12-26 | Способ получения сорбента |
Publications (2)
Publication Number | Publication Date |
---|---|
WO1993012639A2 true WO1993012639A2 (fr) | 1993-07-08 |
WO1993012639A3 WO1993012639A3 (fr) | 1993-08-05 |
Family
ID=21593150
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/UA1992/000001 WO1993012639A2 (fr) | 1991-12-26 | 1992-12-21 | Procede d'obtention d'un sorbant |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU3413793A (fr) |
RU (1) | RU2013120C1 (fr) |
WO (1) | WO1993012639A2 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2476819A (en) * | 2010-01-11 | 2011-07-13 | Univ Surrey | Method for preparing activated charcoal |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2565194C2 (ru) * | 2013-12-30 | 2015-10-20 | Государственное образовательное учреждение высшего профессионального образования "Белгородский государственный университет" | Способ получения сорбента на основе углеродного материала |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3492244A (en) * | 1965-10-13 | 1970-01-27 | Takeda Chemical Industries Ltd | Method for the production of coke |
GB1411264A (en) * | 1971-09-23 | 1975-10-22 | Nihon Jescoal Ind Co Ltd | Process for manufacturing an activated carbon |
GB1545238A (en) * | 1977-11-17 | 1979-05-02 | Univ Malaya | Activated carbon |
GB2086867A (en) * | 1980-10-09 | 1982-05-19 | Univ Pertanian Malaysia | Process for preparing activated carbon |
-
1991
- 1991-12-26 RU SU915019710A patent/RU2013120C1/ru active
-
1992
- 1992-12-21 AU AU34137/93A patent/AU3413793A/en not_active Abandoned
- 1992-12-21 WO PCT/UA1992/000001 patent/WO1993012639A2/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3492244A (en) * | 1965-10-13 | 1970-01-27 | Takeda Chemical Industries Ltd | Method for the production of coke |
GB1411264A (en) * | 1971-09-23 | 1975-10-22 | Nihon Jescoal Ind Co Ltd | Process for manufacturing an activated carbon |
GB1545238A (en) * | 1977-11-17 | 1979-05-02 | Univ Malaya | Activated carbon |
GB2086867A (en) * | 1980-10-09 | 1982-05-19 | Univ Pertanian Malaysia | Process for preparing activated carbon |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2476819A (en) * | 2010-01-11 | 2011-07-13 | Univ Surrey | Method for preparing activated charcoal |
GB2476819B (en) * | 2010-01-11 | 2014-05-07 | Univ Surrey | Activated charcoal |
Also Published As
Publication number | Publication date |
---|---|
WO1993012639A3 (fr) | 1993-08-05 |
RU2013120C1 (ru) | 1994-05-30 |
AU3413793A (en) | 1993-07-28 |
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