CN205995268U - A kind of New Desulphurizers - Google Patents
A kind of New Desulphurizers Download PDFInfo
- Publication number
- CN205995268U CN205995268U CN201620849869.8U CN201620849869U CN205995268U CN 205995268 U CN205995268 U CN 205995268U CN 201620849869 U CN201620849869 U CN 201620849869U CN 205995268 U CN205995268 U CN 205995268U
- Authority
- CN
- China
- Prior art keywords
- duct
- particle body
- sorbent particle
- utility
- circular arc
- 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.)
- Active
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of New Desulphurizers, this sorbent particle body is cylinder, and cylindrical two bottom surfaces are circular arc；Described cylinder bottom surface and side are provided with the duct running through sorbent particle body.Pore passage structure of the present utility model allows gas diffusion to granule, and is difficult in course of reaction to be blocked by product, makes the ratio that desulphurization reaction is carried out more thoroughly, is conducive to improving desulphurization reaction speed and desulfuration efficiency.This utility model has the advantages that specific surface area is big, pore volume is high, porosity is high, mass-and heat-transfer performance is good simultaneously, is conducive to improving Sulfur capacity and desulfurization precision, prospects for commercial application is wide, practical.
Description
Technical field
This utility model belongs to technical field of desulfuration purification and in particular to a kind of New Desulphurizers.
Background technology
Sulfur-containing impurities can be produced during with coal or oil for raw material production chemical products, and such chemical products
Used in production, catalyst is often very sensitive to poisonous substance, and sulfur is one of most common, generally existing poisonous substance it is necessary to effectively
Removing, the normal use of guarantee downstream process catalyst.In addition, when town gas and natural gas use as fuel gas,
Sour gas cognition causes to equipment such as gas turbine blades to corrode；Catalyst sulfur poisoning then can be made as unstripped gas, simultaneously its combustion
Burning is converted into SO2Discharge into the atmosphere and can cause acid rain, serious harm environmental and human health impacts, H therefore in technical process2S
Deng sulphur-containing substance removing be the combustion gas later use such as coal gas, natural gas necessary links.
In industrial chemicals, coal gas, selexol process purification process, the excellent desulfurizing agent of processability is head therein
Will.The desulfurization precision of traditional desulfurizing agent and Sulfur capacity are relatively low, bad mechanical strength, and mass transfer and heat transfer property are poor, are easily saturated, desulfurization
Efficiency is low.
Content of the invention
The purpose of this utility model is, the problem existing for prior art, provides that a kind of specific surface area is big, pore volume
High, porosity is high, mass transfer and heat transfer property is good, desulfurization precision and the high New Desulphurizers of Sulfur capacity.
For achieving the above object, this utility model adopts the technical scheme that：
A kind of New Desulphurizers, wherein, described sorbent particle body is cylinder, and cylindrical two bottom surfaces are circle
Arc；Described cylinder bottom surface and side are provided with the duct running through sorbent particle body.
Preferably, described duct is equally distributed in the bottom surface of described sorbent particle body cylinder and side.
Preferably, the gap 0.5mm between described duct.
Preferably, described duct is circular duct.
Preferably, described duct is square duct or equilateral triangle duct.
Preferably, described circle duct aperture is 200 ~ 800nm.
Preferably, a diameter of 200 ~ 800nm of described square duct or equilateral triangle duct circumscribed circle.
Preferably, the radius of described sorbent particle body cylinder circular arc bottom surface is 4 ~ 9mm.
Preferably, the height of described sorbent particle body cylinder and circular arc bottom surface radius ratio are 1:1~3:1.
Preferably, described sorbent particle body cylinder circular arc bottom surface and the angle of horizontal plane are 20°~50°.
The beneficial effects of the utility model are：
（1）Large aperture pore passage structure that this utility model sorbent particle body is provided through it is allowed to gas diffusion extremely
Inside granule, and it is difficult in course of reaction to be blocked by product, makes the ratio that desulphurization reaction is carried out more thoroughly, be conducive to improving
Desulphurization reaction speed and desulfuration efficiency.
（2）This utility model also has the advantages that specific surface area is big, pore volume is high, porosity is high, mass-and heat-transfer performance is good,
Be conducive to improving Sulfur capacity and desulfurization precision, prospects for commercial application is wide, practical.
Brief description
Fig. 1 is the main structure diagram of this utility model one embodiment.
Fig. 2 is the overlooking the structure diagram of this utility model one embodiment.
Fig. 3 is the cross-sectional view of this utility model one embodiment.
Specific embodiment
With specific embodiment, technical solutions of the utility model are described in detail below in conjunction with the accompanying drawings, with further
Understand the purpose of this utility model, scheme and effect, but be not limited to this utility model.
Embodiment 1
With reference to Fig. 1 ~ 3, a kind of New Desulphurizers, wherein, described sorbent particle body is cylinder 1, two of cylinder 1
Bottom surface is circular arc；Described cylinder bottom surface and side are provided with the duct 2 running through sorbent particle body.
Described duct is equally distributed in the bottom surface of described sorbent particle body cylinder and side.
Gap between described duct is 0.5mm.
Described duct is circular duct.
Described circle duct aperture is 200nm.
The radius of described sorbent particle body cylinder circular arc bottom surface is 4mm.
The height of described sorbent particle body cylinder 1 and circular arc bottom surface radius ratio are 1:1.
Described sorbent particle body cylinder circular arc bottom surface is 20 with the angle of horizontal plane°.
Embodiment 2
The present embodiment is with the difference of embodiment 1, and the duct of the present embodiment is square duct, and square duct is external
Diameter of a circle is 200nm, and sorbent particle body cylinder circular arc bottom surface is 50 with the angle of horizontal plane°.
Embodiment 3
The present embodiment is with the difference of embodiment 1, and the duct of the present embodiment is equilateral triangle duct, equilateral triangle duct
A diameter of 800nm of circumscribed circle, sorbent particle body cylinder circular arc bottom surface with the angle of horizontal plane is, 45°.
Embodiment 4
Difference with embodiment 1 is, the present embodiment circle duct aperture is 800nm, sorbent particle body cylinder
Height and circular arc bottom surface radius ratio be 3:1, the radius of sorbent particle body cylinder circular arc bottom surface is 9mm.
Embodiment 5
Difference with embodiment 1 is, the present embodiment circle duct aperture is 500nm, sorbent particle body cylinder
Height and circular arc bottom surface radius ratio be 2:1, the radius of sorbent particle body cylinder circular arc bottom surface is 5mm.
Above example only in order to the technical solution of the utility model to be described and unrestricted, although with reference to preferred embodiment pair
This utility model has been described in detail, it will be understood by those within the art that, can be to technology of the present utility model
Scheme is modified or equivalent, the objective without deviating from technical solutions of the utility model and scope, and it all should be covered
In the middle of right of the present utility model.
Claims (10)
1. a kind of New Desulphurizers it is characterised in that：Described sorbent particle body is cylinder, and cylindrical two bottom surfaces are equal
For circular arc；Described cylinder bottom surface and side are provided with the duct running through sorbent particle body.
2. New Desulphurizers according to claim 1 it is characterised in that：Described duct is justified in described sorbent particle body
The bottom surface of cylinder and side are equally distributed.
3. New Desulphurizers according to claim 1 it is characterised in that：Gap 0.5mm between described duct.
4. New Desulphurizers according to claim 1 and 2 it is characterised in that：Described duct is circular duct.
5. New Desulphurizers according to claim 3 it is characterised in that：Described duct is square duct or positive triangle
Shape duct.
6. New Desulphurizers according to claim 4 it is characterised in that：Described circle duct aperture is 200 ~ 800nm.
7. New Desulphurizers according to claim 5 it is characterised in that：Described square duct or equilateral triangle duct
A diameter of 200 ~ 800nm of circumscribed circle.
8. New Desulphurizers according to claim 1 it is characterised in that：Described sorbent particle body cylinder circular arc
The radius of bottom surface is 4 ~ 9mm.
9. New Desulphurizers according to claim 1 it is characterised in that：The height of described sorbent particle body cylinder
It is 1 with circular arc bottom surface radius ratio:1~3:1.
10. New Desulphurizers according to claim 1 it is characterised in that：Described sorbent particle body cylinder circular arc
Shape bottom surface is 20 with the angle of horizontal plane°~50°.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620849869.8U CN205995268U (en) | 2016-08-08 | 2016-08-08 | A kind of New Desulphurizers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620849869.8U CN205995268U (en) | 2016-08-08 | 2016-08-08 | A kind of New Desulphurizers |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205995268U true CN205995268U (en) | 2017-03-08 |
Family
ID=58200430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620849869.8U Active CN205995268U (en) | 2016-08-08 | 2016-08-08 | A kind of New Desulphurizers |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205995268U (en) |
-
2016
- 2016-08-08 CN CN201620849869.8U patent/CN205995268U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102092688A (en) | Technological process for producing acid with sulfur-containing gas | |
| CN102120179B (en) | Preparation method of modified activated carbon fiber for adsorbing ultra-micro sulfur dioxide | |
| CN204768110U (en) | Promote mercury and fine particles device of desorption in coordination among wet flue gas desulfurization | |
| CN203043799U (en) | Acid mist purification tower | |
| CN201930706U (en) | Simple boiler desulfurizing and dedusting system | |
| CN205995268U (en) | A kind of New Desulphurizers | |
| CN202199448U (en) | Spray head | |
| CN205796820U (en) | A kind of desulfurating dust-removing equipment | |
| CN104941379A (en) | Method and device for promoting simultaneous removal of mercury and fine particulate matters during wet flue gas desulfurization | |
| CN108993133A (en) | COS, CS in a kind of promotion natural gas2The method of removing | |
| CN203663675U (en) | Multifunctional phenol waste gas purification device | |
| CN107469797B (en) | A kind of preparation method of the modified porous magnetic composite microsphere of dimercaptosuccinic acid | |
| CN203737097U (en) | Flue gas desulphurization system of industrial boiler | |
| CN101862639A (en) | Preparation method of modified activated carbon fiber loaded metal ion methane desulfurizer | |
| CN205392157U (en) | Hydrogen sulfide gas body absorption test device | |
| CN213348372U (en) | Desulfurizing tower for acidolysis tail gas | |
| CN103357376A (en) | Nano-grade attapulgite substrate SO2 absorption agent preparation method | |
| CN203845819U (en) | Manufacturing system of low-dewpoint nitrogen for lithium battery | |
| CN203694875U (en) | Radial cross-flow moving-bed reactor for removal of hydrogen sulfide by temperature swing adsorption | |
| CN208757252U (en) | A kind of desulfurizer that may be reused | |
| CN102527183A (en) | Desulfurization device special for oil burning boiler | |
| CN106118777A (en) | A kind of marsh gas purifying purifies the method for methane | |
| CN204522694U (en) | Novel three-in-one multifunctional fume desulfurizing tower | |
| CN203329595U (en) | Novel flue gas desulfurization tower | |
| CN103768892A (en) | Radial cross-flow moving bed reactor for adsorbing and removing hydrogen sulfide at variable temperature |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |