CN205659976U - Fusion method industry sodium chloride abraum salt treatment facility - Google Patents
Fusion method industry sodium chloride abraum salt treatment facility Download PDFInfo
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- CN205659976U CN205659976U CN201620534433.XU CN201620534433U CN205659976U CN 205659976 U CN205659976 U CN 205659976U CN 201620534433 U CN201620534433 U CN 201620534433U CN 205659976 U CN205659976 U CN 205659976U
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Abstract
The utility model relates to a fusion method industry sodium chloride abraum salt treatment facility belongs to the organic by -product salt treatment facility technical field of solid. Including pyrolysis oven, electric heater unit, combustion chamber, its characterized in that, the pyrolysis oven set up electric heater unit, the pyrolysis oven sets up a plurality of organic by -product salt entry, furnace one side sets up the fused salt export, the combustion chamber on be provided with exhanst gas outlet, purification salt export and fused salt import respectively, fused salt import and pyrolysis oven on the fused salt exit linkage. The utility model discloses fine solution the problem that the organic matter was left over in organic by -product salt, finally realize the innocent treatment of organic by -product salt, adopt this device when reaching the organic by -product salt of purification, effectual production of stopping noxious material such as dioxin can not lead to the fact the environmental pollution and the wasting of resources, produces economic benefits simultaneously.
Description
Technical field
This utility model belongs to SOLID ORGANIC by-product salt treatment equipment technical field, is specifically related to a kind of fusion method industry chlorine
Change sodium abraum salt processing equipment.
Background technology
The a lot of enterprise of Fine Chemical can produce abraum salt solution in process of production, and be mingled with in abraum salt solution various has more
The impurity such as machine, owing to impurity and salt mix, after abraum salt being separated even with evaporating and concentrating process, it is also difficult to profit again
With because in chemical process use large amount of organic composition, finally have partial organic substances be entrained in salt formed organic
By-product salt, organic by-product salt, only as fixed-end forces, is wasted resource, is returned environment simultaneously and bring the biggest harm.
At present, the method processing organic by-product salt is most commonly used that high-temperature processing method, utilizes high-temperature hot-air calcining and decomposing
Organic principle, but, this kind of method is not only difficult to the organic principle in fully erased abraum salt, and significant portion organic principle turns
Turn to increasingly complex organic component and remain in hot blast, define again new pollutant, in addition it is also necessary to put into high expense and enter
Row processes.It addition, mostly there is the problems such as energy consumption is high, combustion rate is low in the high-temperature cracking furnace processing abraum salt.
Summary of the invention
The purpose of this utility model is to provide a kind of device processing SOLID ORGANIC abraum salt, and this device uses electrical heating with exhausted
The pyrolysis oven of oxygen pyrolysis, while reaching to purify organic by-product salt, effectively stops the generation of the noxious substances such as two English.
The concrete technical scheme that this utility model uses is as follows: a kind of fusion method industrial chlorinations sodium abraum salt processing equipment, bag
Including pyrolysis oven, electric heater unit, combustor, described pyrolysis oven arranges electric heater unit, and pyrolysis oven arranges some organic by-products
Salt entrance, burner hearth side arranges fused salt outlet；It is respectively arranged with exhanst gas outlet on described combustor, purifies salt outlet and fused salt
Import, described fused salt import exports with the fused salt on pyrolysis oven and is connected.
Wherein preferred version is:
The burner hearth of described pyrolysis oven is that ellipse envelope crouches pot, and burner hearth side ellipse head arranges fused salt outlet.
Described electric heater unit is arranged on around the hearth outer wall of pyrolysis oven and bottom pyrolysis oven.
Described top of combustion chamber arranges exhanst gas outlet, and bottom arranges purification salt outlet, and sidewall arranges fused salt import.
Described exhanst gas outlet arranges the follow-up flue gas washing absorption tower of connection.
The beneficial effects of the utility model are:
1, the problem that during this utility model well solves organic by-product salt, Organic substance is left over, finally realizes organic by-product
The harmless treatment of salt；
2, in this device, pyrolysis oven pyrolysis is pyrolyzed for anoxybiotic, and the small-molecule substance after pyrolysis the most fully burns,
Effectively prevent the generation of the harmful substances such as two English；
3, purifying while organic by-product salt, solve organic impurities bring into hot blast is formed again new pollutant this
One difficult problem；
4, the heater of pyrolysis oven is electric heater unit, uses Electric heating to heat organic by-product salt, will not bring into
New impurity, clean energy and the thermal efficiency are high；
5, use this utility model to process SOLID ORGANIC by-product salt and do not result in environmental pollution and the wasting of resources, produce simultaneously
Economic benefit.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model specific embodiment.
In Fig. 1,1-pyrolysis oven, 2-electric heater unit, 3-organic by-product salt entrance, 4-fused salt exports, and 5-combustor, 6-carries
Pure salt exports, 7-exhanst gas outlet, 8-fused salt import.
Detailed description of the invention
As it is shown in figure 1, a kind of fusion method industrial chlorinations sodium abraum salt processing equipment, including pyrolysis oven 1, electric heater unit 2, combustion
Burn room 5.The burner hearth of pyrolysis oven 1 is that ellipse envelope crouches pot, and the roof of the furnace of pyrolysis oven 1 arranges 3 organic by-product salt entrances 3, burner hearth
Fused salt outlet 4 is set on the ellipse head of side.
Electric heater unit 2 is arranged on around the hearth outer wall of pyrolysis oven 1 and bottom pyrolysis oven.
Combustor 5 top arranges exhanst gas outlet 7, and bottom arranges purification salt outlet 6, and sidewall arranges fused salt import 8, and fused salt enters
Mouth 8 exports 4 with the fused salt on pyrolysis oven 1 and is connected.
Fusion method industrial chlorinations sodium abraum salt processing equipment also includes follow-up flue gas washing absorption tower, and follow-up flue gas washing absorbs
Tower is connected with exhanst gas outlet 7.
This utility model processes the method for SOLID ORGANIC by-product salt: in pyrolysis oven 1, is not passed through air, passes through electrical heating
Device 2 is heated to 1000-1200 DEG C, and organic by-product salt is anoxybiotic pyrolysis in pyrolysis oven 1, from fused salt outlet 4 inflow combustion after pyrolysis
Burning room 5, the harmful substance in organic by-product salt fully burns in combustor 5, and flue gas enters follow-up flue gas through exhanst gas outlet 7 and washes
Washing absorption tower, washing after-purification reaches discharge standard and collects through smoke stack emission, purification salt purified salt outlet 6, and high-temperature flue gas enters
Row waste heat recovery.
Claims (5)
1. a fusion method industrial chlorinations sodium abraum salt processing equipment, including pyrolysis oven, electric heater unit, combustor, its feature exists
In,
Described pyrolysis oven arranges electric heater unit, and pyrolysis oven arranges some organic by-product salt entrances, and burner hearth side arranges fused salt
Outlet；
It is respectively arranged with exhanst gas outlet on described combustor, purifies salt outlet and fused salt import, described fused salt import and heat
The fused salt outlet solved on stove connects.
Fusion method industrial chlorinations sodium abraum salt processing equipment the most according to claim 1, it is characterised in that described pyrolysis oven
Burner hearth be that ellipse envelope crouches pot, burner hearth side ellipse head arranges fused salt outlet.
Fusion method industrial chlorinations sodium abraum salt processing equipment the most according to claim 1, it is characterised in that described electrical heating
Device is arranged on around the hearth outer wall of pyrolysis oven and bottom pyrolysis oven.
Fusion method industrial chlorinations sodium abraum salt processing equipment the most according to claim 1, it is characterised in that described combustor
Top arranges exhanst gas outlet, and bottom arranges purification salt outlet, and sidewall arranges fused salt import.
5. according to the fusion method industrial chlorinations sodium abraum salt processing equipment described in claim 1 or 4, it is characterised in that described cigarette
Gas outlet arranges the follow-up flue gas washing absorption tower of connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620534433.XU CN205659976U (en) | 2016-06-02 | 2016-06-02 | Fusion method industry sodium chloride abraum salt treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620534433.XU CN205659976U (en) | 2016-06-02 | 2016-06-02 | Fusion method industry sodium chloride abraum salt treatment facility |
Publications (1)
| Publication Number | Publication Date |
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| CN205659976U true CN205659976U (en) | 2016-10-26 |
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| CN201620534433.XU Active CN205659976U (en) | 2016-06-02 | 2016-06-02 | Fusion method industry sodium chloride abraum salt treatment facility |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107128951A (en) * | 2017-06-22 | 2017-09-05 | 南京诚朴环保科技有限公司 | A kind of method of organic matter in removing inorganic salts |
| CN107726851A (en) * | 2017-11-07 | 2018-02-23 | 重庆恒瑞窑炉工程有限公司 | A kind of stove and method that the useless danger sodium chloride of chemical industry is converted into refining industrial salt |
| CN109250732A (en) * | 2017-07-13 | 2019-01-22 | 南京诚朴环保科技有限公司 | A kind of cooling means of inorganic molten salt |
| CN109865734A (en) * | 2019-03-13 | 2019-06-11 | 兰州有色冶金设计研究院有限公司 | A method of vitreum is produced using chemical industry abraum salt |
| CN111790731A (en) * | 2020-07-20 | 2020-10-20 | 杭州碳氢科技研究有限公司 | Industrial waste salt conversion device and method |
| CN112474720A (en) * | 2020-11-09 | 2021-03-12 | 宿迁安湘环保科技有限公司 | Method for separating low-temperature inorganic salt in hazardous waste |
| CN114101298A (en) * | 2021-11-22 | 2022-03-01 | 内蒙古中泰汇金环保科技有限公司 | Heat treatment method of high-content organic mixed salt |
-
2016
- 2016-06-02 CN CN201620534433.XU patent/CN205659976U/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107128951A (en) * | 2017-06-22 | 2017-09-05 | 南京诚朴环保科技有限公司 | A kind of method of organic matter in removing inorganic salts |
| CN107128951B (en) * | 2017-06-22 | 2019-07-12 | 南京诚朴环保科技有限公司 | A kind of method of organic matter in removing inorganic salts |
| CN109250732A (en) * | 2017-07-13 | 2019-01-22 | 南京诚朴环保科技有限公司 | A kind of cooling means of inorganic molten salt |
| CN109250732B (en) * | 2017-07-13 | 2020-12-04 | 南京诚朴环保科技有限公司 | Cooling method of inorganic molten salt |
| CN107726851A (en) * | 2017-11-07 | 2018-02-23 | 重庆恒瑞窑炉工程有限公司 | A kind of stove and method that the useless danger sodium chloride of chemical industry is converted into refining industrial salt |
| CN109865734A (en) * | 2019-03-13 | 2019-06-11 | 兰州有色冶金设计研究院有限公司 | A method of vitreum is produced using chemical industry abraum salt |
| CN111790731A (en) * | 2020-07-20 | 2020-10-20 | 杭州碳氢科技研究有限公司 | Industrial waste salt conversion device and method |
| CN111790731B (en) * | 2020-07-20 | 2023-07-18 | 杭州碳氢科技研究有限公司 | Industrial waste salt conversion device and method |
| CN112474720A (en) * | 2020-11-09 | 2021-03-12 | 宿迁安湘环保科技有限公司 | Method for separating low-temperature inorganic salt in hazardous waste |
| CN114101298A (en) * | 2021-11-22 | 2022-03-01 | 内蒙古中泰汇金环保科技有限公司 | Heat treatment method of high-content organic mixed salt |
| CN114101298B (en) * | 2021-11-22 | 2023-08-04 | 内蒙古中泰汇金环保科技有限公司 | Heat treatment method for high-content organic hetero salt |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190930 Address after: 255086 12-storey Advanced Ceramic Innovation Park 125 Liuquan Road, Zibo High-tech Zone, Shandong Province Co-patentee after: Liu Yanqiu Patentee after: Yang De Cheng Co-patentee after: Wei Ruizhu Address before: 255086 Shandong city of Zibo province high tech Zone Willow Road No. 125 advanced ceramics science and Technology Innovation Park 12 Patentee before: SHANDONG ZHONGTIAN INTERNATIONAL ENGINEERING CO., LTD. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201229 Address after: Room 1101, block B, advanced ceramic technology innovation park, 125 Liuquan Road, high tech Zone, Zibo City, Shandong Province Patentee after: SHANDONG ZHONGTIAN TECHNOLOGY & ENGINEERING Co.,Ltd. Address before: 255086 12th floor, advanced ceramic Innovation Park, 125 Liuquan Road, high tech Zone, Zibo City, Shandong Province Patentee before: Yang Decheng Patentee before: Liu Yanqiu Patentee before: Wei Ruizhu |