CN107128916A - A kind of sugar industry activated carbon - Google Patents
A kind of sugar industry activated carbon Download PDFInfo
- Publication number
- CN107128916A CN107128916A CN201710266122.9A CN201710266122A CN107128916A CN 107128916 A CN107128916 A CN 107128916A CN 201710266122 A CN201710266122 A CN 201710266122A CN 107128916 A CN107128916 A CN 107128916A
- Authority
- CN
- China
- Prior art keywords
- parts
- activated carbon
- carbide
- raw material
- sugar industry
- Prior art date
- 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.)
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Classifications
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- 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
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/90—Other properties not specified above
Abstract
The present invention relates to a kind of sugar industry activated carbon, using coal or hard fruit shell as raw material, charing process is carried out after raw material is crushed, room temperature is subsequently cooled to, obtains carbide;Carbide is placed in maceration extract and soaks 6 8h, is then dried, the carbide after being impregnated;Carbide after dipping is subjected to activation process, then post-processed, finally sieves, produces;The maceration extract be by 100 parts of water, 45 parts of concentration for 37% hydrochloric acid, 56 parts of zinc oxide, 68 parts of potassium hydroxide mix.The activated carbon protects ecological environment not using timber as raw material, and to the good decolorizing effect of sugar products, extensively, cost is low for raw material sources.
Description
Technical field
The present invention relates to a kind of activated carbon, especially a kind of activated carbon for sugar industry, belong to fine chemical technology
Field.
Background technology
In the last few years, the quality requirement more and more higher of the domestic sugar products to sugar industry, the peace and quiet effect of activated carbon compared with
It is good, therefore be widely used.In the prior art, sugar industry uses 10 more with using timber for raw material activated carbon with sugar charcoal per ton
Cube timber is raw material, and China produces all size sugar charcoal per year in terms of 30,000 tons (accounting for total 6 of charcoal amount 1), about needs 300,000 cubes of timber, this
Undoubtedly a large amount of forests will be caused to be cut down, heavy damage is ecological.
The content of the invention
There is provided one kind sugaring work for the deficiency existed present invention aim to address sugar industry activated carbon in the prior art
Industry activated carbon, it is not using timber as raw material, and to the good decolorizing effect of sugar products.
Technical scheme
A kind of sugar industry activated carbon, is prepared from by the following method:
(1) using coal or hard fruit shell as raw material, charing process is carried out after raw material is crushed, room temperature is subsequently cooled to, obtains
To carbide;
(2) maceration extract is prepared, carbide is placed in maceration extract and soaks 6-8h, is then dried, the charing after being impregnated
Thing;
(3) carbide after dipping is subjected to activation process, then post-processed, finally sieved, produce;
In step (2), the maceration extract is hydrochloric acid, 5-6 parts of zinc oxide, the 6-8 by 100 parts of water, 4-5 parts of concentration for 37%
Part potassium hydroxide is mixed, and the number is parts by weight.
Further, in step (1), the charing process refers to raw material isolation air heating 2-4h at 300-400 DEG C.
Further, the maceration extract is hydrochloric acid, 5 parts of zinc oxide, the 8 parts of hydroxides by 100 parts of water, 5 parts of concentration for 37%
Potassium is mixed.
Further, in step (2), the drying temperature is 200-300 DEG C, and the time is 2-4h.
Further, in step (3), the activation temperature is 650-750 DEG C, and the time is 6-10h.
Further, in step (3), the post processing includes pickling, washing, drying successively.
Beneficial effects of the present invention:The activated carbon of the present invention, it protects ecological environment not using timber as raw material, and
To the good decolorizing effect of sugar products, extensively, cost is low for raw material sources.
Embodiment
With reference to embodiment, the invention will be further described.
Embodiment 1
It will be put into after 100kg coal crushings in Muffle furnace and heat 3h in 400 DEG C, be subsequently cooled to room temperature, obtain carbide;
Prepare maceration extract:Mixed, will be carbonized for 37% hydrochloric acid, 5kg zinc oxide, 8kg potassium hydroxide by 100kg water, 5kg concentration
Thing, which is placed in maceration extract, soaks 6h, then 250 DEG C of baking 4h, the carbide after being impregnated;By the carbide after dipping at 700 DEG C
Activation process 8h, then with watery hydrochloric acid pickling, be washed to neutrality again, finally dry, sieve, produce.
Embodiment 2
100kg palm shells are put into Muffle furnace and heat 4h in 350 DEG C, room temperature is cooled to, obtains carbide;Prepare dipping
Liquid:Mixed by 100kg water, 5kg concentration for 37% hydrochloric acid, 5kg zinc oxide, 8kg potassium hydroxide, carbide is placed in leaching
8h is soaked in stain liquid, then 300 DEG C of baking 4h, the carbide after being impregnated;By the carbide after dipping in 650 DEG C of activation process
10h, then with watery hydrochloric acid pickling, be washed to neutrality again, finally dry, sieve, produce.
Embodiment 3
100kg coconut husks are put into Muffle furnace and heat 3h in 380 DEG C, room temperature is cooled to, obtains carbide;Prepare dipping
Liquid:Mixed by 100kg water, 4kg concentration for 37% hydrochloric acid, 6kg zinc oxide, 8kg potassium hydroxide, carbide is placed in leaching
7h is soaked in stain liquid, then 300 DEG C of baking 4h, the carbide after being impregnated;By the carbide after dipping in 680 DEG C of activation process
6h, then with watery hydrochloric acid pickling, be washed to neutrality again, finally dry, sieve, produce.
Decoloration active carbon made from embodiment is carried out into iodine sorption value, mechanical strength and caramel to decolourize to test, be the results are shown in Table
1:
Table 1
Iodine sorption value (mg/g) | Mechanical strength (%) | Caramel decolorization rate (%) | |
Embodiment 1 | 1150 | 97 | 92 |
Embodiment 2 | 1020 | 98 | 93 |
Embodiment 3 | 990 | 95 | 89 |
Claims (6)
1. a kind of sugar industry activated carbon, it is characterised in that be prepared from by the following method:
(1) using coal or hard fruit shell as raw material, charing process is carried out after raw material is crushed, room temperature is subsequently cooled to, obtains charcoal
Compound;
(2) maceration extract is prepared, carbide is placed in maceration extract and soaks 6-8h, is then dried, the carbide after being impregnated;
(3) carbide after dipping is subjected to activation process, then post-processed, finally sieved, produce;
In step (2), the maceration extract is hydrochloric acid, 5-6 parts of zinc oxide, the 6-8 parts of hydrogen by 100 parts of water, 4-5 parts of concentration for 37%
Potassium oxide is mixed, and the number is parts by weight.
2. sugar industry activated carbon as claimed in claim 1, it is characterised in that in step (1), the charing process refers to
Raw material isolation air is heated into 2-4h at 300-400 DEG C.
3. sugar industry activated carbon as claimed in claim 1, it is characterised in that the maceration extract be by 100 parts of water, 5 parts
Concentration for 37% hydrochloric acid, 5 parts of zinc oxide, 8 parts of potassium hydroxide mix.
4. sugar industry activated carbon as claimed in claim 1, it is characterised in that in step (2), the drying temperature is
200-300 DEG C, the time is 2-4h.
5. sugar industry activated carbon as claimed in claim 1, it is characterised in that in step (3), the activation temperature is
650-750 DEG C, the time is 6-10h.
6. the sugar industry activated carbon as described in any one of claim 1 to 5, it is characterised in that in step (3), it is described after
Processing includes pickling, washing, drying successively.
Priority Applications (1)
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CN201710266122.9A CN107128916A (en) | 2017-04-21 | 2017-04-21 | A kind of sugar industry activated carbon |
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CN201710266122.9A CN107128916A (en) | 2017-04-21 | 2017-04-21 | A kind of sugar industry activated carbon |
Publications (1)
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CN107128916A true CN107128916A (en) | 2017-09-05 |
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CN201710266122.9A Pending CN107128916A (en) | 2017-04-21 | 2017-04-21 | A kind of sugar industry activated carbon |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107792853A (en) * | 2017-11-28 | 2018-03-13 | 福建省鑫森炭业股份有限公司 | A kind of high intensity granular activated carbon for liquid phase desorption and preparation method thereof |
CN111762780A (en) * | 2020-05-06 | 2020-10-13 | 宁夏银建卡奔活性炭有限公司 | Special carbon for treating organic gas in urban underground water |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101054176A (en) * | 2007-03-09 | 2007-10-17 | 朝阳森塬活性炭有限公司 | Granule decoloration active carbon and preparation method thereof |
CN104445190A (en) * | 2013-09-13 | 2015-03-25 | 中国科学院兰州化学物理研究所 | Method for preparation of activated carbon with high specific surface area by using asparagus lettuce leaf as carbon source |
-
2017
- 2017-04-21 CN CN201710266122.9A patent/CN107128916A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101054176A (en) * | 2007-03-09 | 2007-10-17 | 朝阳森塬活性炭有限公司 | Granule decoloration active carbon and preparation method thereof |
CN104445190A (en) * | 2013-09-13 | 2015-03-25 | 中国科学院兰州化学物理研究所 | Method for preparation of activated carbon with high specific surface area by using asparagus lettuce leaf as carbon source |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107792853A (en) * | 2017-11-28 | 2018-03-13 | 福建省鑫森炭业股份有限公司 | A kind of high intensity granular activated carbon for liquid phase desorption and preparation method thereof |
CN111762780A (en) * | 2020-05-06 | 2020-10-13 | 宁夏银建卡奔活性炭有限公司 | Special carbon for treating organic gas in urban underground water |
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