CN108928818A - A kind of production technology of active carbon - Google Patents

A kind of production technology of active carbon Download PDF

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Publication number
CN108928818A
CN108928818A CN201810705685.8A CN201810705685A CN108928818A CN 108928818 A CN108928818 A CN 108928818A CN 201810705685 A CN201810705685 A CN 201810705685A CN 108928818 A CN108928818 A CN 108928818A
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CN
China
Prior art keywords
raw material
active carbon
retort
furnace
furnace temperature
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.)
Pending
Application number
CN201810705685.8A
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Chinese (zh)
Inventor
胡峰
李修龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xuzhou Sen Furniture Co Ltd
Original Assignee
Xuzhou Sen Furniture Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xuzhou Sen Furniture Co Ltd filed Critical Xuzhou Sen Furniture Co Ltd
Priority to CN201810705685.8A priority Critical patent/CN108928818A/en
Publication of CN108928818A publication Critical patent/CN108928818A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • C01B32/312Preparation
    • C01B32/318Preparation characterised by the starting materials
    • C01B32/324Preparation characterised by the starting materials from waste materials, e.g. tyres or spent sulfite pulp liquor
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • C01B32/312Preparation
    • C01B32/336Preparation characterised by gaseous activating agents

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

The invention discloses a kind of production technologies of active carbon, the following steps are included: (1) prepares, raw material, (2) carry out carbonization treatment to raw material, (3) crush, examine, are packed and stored, the sources that the present invention has sufficiently used the plant resources such as timber, sawdust, tree root, fruit stone, shell, widened activated carbon raw material, reduce the cost of material of active carbon, and method for preparation of active carbon of the present invention is easy, time-consuming shorter, and manufactured active carbon finished products quality is higher.

Description

A kind of production technology of active carbon
Technical field
The present invention relates to technical field of active carbon, in particular to a kind of production technologies of active carbon.
Background technique
Active carbon, also known as activated carbon, activated carbon or activated carbon are black powder or granular carbonizable substance.Active carbon Since microcrystalline carbon is irregular alignment in structure, there is pore between interconnection, carbon tissue defects can be generated in activation, Therefore it is a kind of porous carbon, and bulk density is low, large specific surface area, and does the main material of a filter.Existing work Property charcoal preparation process is complicated, raw material expend larger, there are some problems in actual production.
Summary of the invention
In order to solve the above technical problems, technical solution provided by the invention are as follows: a kind of production technology of active carbon, including with Lower step:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell are put into furnace vehicle by raw material mixed grinding, and by raw material, And furnace vehicle is put into retort.
(2) retort is warming up to 20~150 DEG C, the moisture evaporation for adhering to raw material surface;Charing furnace temperature is risen to 175~275 DEG C, raw material is made to enter pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Charing furnace temperature is risen to 300~400 DEG C, carbonize raw material, and be passed through vapor into retort and reacted;Charing furnace temperature is risen to 450~550 DEG C, Calcine raw material, the impurity of discharge residual in the feed.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, put after cooling Enter pulverizer to crush, examine, be packed and stored.
The present invention has sufficiently used the plant resources such as timber, sawdust, tree root, fruit stone, shell, has widened activated carbon raw material Sources reduce the cost of material of active carbon, and method for preparation of active carbon of the present invention is easy, time-consuming shorter, manufactured Active carbon finished products quality is higher.
Specific embodiment
Embodiment one
A kind of production technology of active carbon, which comprises the following steps:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell are put into furnace vehicle by raw material mixed grinding, and by raw material, And furnace vehicle is put into retort.
(2) retort is warming up to 20~150 DEG C, the moisture evaporation for adhering to raw material surface;Charing furnace temperature is risen to 175 DEG C, raw material is made to enter pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Will charing furnace temperature rise to 300 DEG C, make raw material into Row charing, and be passed through vapor into retort and reacted;Charing furnace temperature is risen to 450 DEG C, raw material is calcined, arranges Impurity in the feed is remained out.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, put after cooling Enter pulverizer to crush, examine, be packed and stored.
Embodiment two
A kind of production technology of active carbon, which comprises the following steps:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell are put into furnace vehicle by raw material mixed grinding, and by raw material, And furnace vehicle is put into retort.
(2) retort is warming up to 150 DEG C, the moisture evaporation for adhering to raw material surface;Charing furnace temperature is risen to 275 DEG C, so that raw material is entered pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Charing furnace temperature is risen to 400 DEG C, raw material is made to carry out charcoal Change, and is passed through vapor into retort and is reacted;Charing furnace temperature is risen to 550 DEG C, raw material is calcined, is discharged residual Stay impurity in the feed.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, put after cooling Enter pulverizer to crush, examine, be packed and stored.
Embodiment three
A kind of production technology of active carbon, which comprises the following steps:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell are put into furnace vehicle by raw material mixed grinding, and by raw material, And furnace vehicle is put into retort.
(2) retort is warming up to 100 DEG C, the moisture evaporation for adhering to raw material surface;Charing furnace temperature is risen to 200 DEG C, so that raw material is entered pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Charing furnace temperature is risen to 350 DEG C, raw material is made to carry out charcoal Change, and is passed through vapor into retort and is reacted;Charing furnace temperature is risen to 500 DEG C, raw material is calcined, is discharged residual Stay impurity in the feed.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, put after cooling Enter pulverizer to crush, examine, be packed and stored.
Example IV
A kind of production technology of active carbon, which comprises the following steps:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell are put into furnace vehicle by raw material mixed grinding, and by raw material, And furnace vehicle is put into retort.
(2) retort is warming up to 80 DEG C, the moisture evaporation for adhering to raw material surface;Charing furnace temperature is risen to 220 DEG C, So that raw material is entered pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Charing furnace temperature is risen to 370 DEG C, carbonizes raw material, And vapor is passed through into retort and is reacted;Charing furnace temperature is risen to 500 DEG C, calcines raw material, discharge residual Impurity in the feed.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, put after cooling Enter pulverizer to crush, examine, be packed and stored.
Above-mentioned detailed description is an example of the present invention, the patent that above embodiment is not intended to limit the invention Range, it is all without departing from equivalence enforcement or change of the invention, it is intended to be limited solely by the scope of the patents of the invention.

Claims (1)

1. a kind of production technology of active carbon, which comprises the following steps:
(1) prepare raw material: timber, sawdust, tree root, fruit stone, shell, be put into furnace vehicle by raw material mixed grinding, and by raw material, and will Furnace vehicle is put into retort.
(2) retort is warming up to 20~150 DEG C, the moisture evaporation for adhering to raw material surface;Will charing furnace temperature rise to 175~ 275 DEG C, raw material is made to enter pre- carbonization stage, raw material is made to carry out pyrolytic reaction;Charing furnace temperature is risen to 300~400 DEG C, makes original Material is carbonized, and is passed through vapor into retort and is reacted;Will charing furnace temperature rise to 450~550 DEG C, make raw material into Row calcining, the impurity of discharge residual in the feed.
(3) active carbon that reaction obtains is entered in discharging cooler by the discharge port of furnace tail and is cooled down, be put into powder after cooling Broken machine is crushed, examines, is packed and stored.
CN201810705685.8A 2018-07-02 2018-07-02 A kind of production technology of active carbon Pending CN108928818A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810705685.8A CN108928818A (en) 2018-07-02 2018-07-02 A kind of production technology of active carbon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810705685.8A CN108928818A (en) 2018-07-02 2018-07-02 A kind of production technology of active carbon

Publications (1)

Publication Number Publication Date
CN108928818A true CN108928818A (en) 2018-12-04

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810705685.8A Pending CN108928818A (en) 2018-07-02 2018-07-02 A kind of production technology of active carbon

Country Status (1)

Country Link
CN (1) CN108928818A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627066A (en) * 2019-11-04 2019-12-31 浙江农林大学 Method for preparing heteroatom-doped porous carbon by using biomass waste as activating agent
CN115465861A (en) * 2022-09-29 2022-12-13 江西李氏烤鲜竹沥药业有限公司 Method for preparing activated carbon by continuous carbonization

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627066A (en) * 2019-11-04 2019-12-31 浙江农林大学 Method for preparing heteroatom-doped porous carbon by using biomass waste as activating agent
CN110627066B (en) * 2019-11-04 2020-12-29 浙江农林大学 Method for preparing heteroatom-doped porous carbon by using biomass waste as activating agent
CN115465861A (en) * 2022-09-29 2022-12-13 江西李氏烤鲜竹沥药业有限公司 Method for preparing activated carbon by continuous carbonization

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Application publication date: 20181204

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