CN205516623U - Molecular sieve drying tower - Google Patents
Molecular sieve drying tower Download PDFInfo
- Publication number
- CN205516623U CN205516623U CN201620063781.3U CN201620063781U CN205516623U CN 205516623 U CN205516623 U CN 205516623U CN 201620063781 U CN201620063781 U CN 201620063781U CN 205516623 U CN205516623 U CN 205516623U
- Authority
- CN
- China
- Prior art keywords
- tower body
- tubulation
- connecting plate
- upper junction
- molecular sieve
- 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.)
- Expired - Fee Related
Links
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 19
- 238000001035 drying Methods 0.000 title claims abstract description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000011344 liquid material Substances 0.000 claims abstract description 14
- 230000008676 import Effects 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 12
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 229910001873 dinitrogen Inorganic materials 0.000 abstract 4
- 230000004913 activation Effects 0.000 abstract 1
- 230000008929 regeneration Effects 0.000 abstract 1
- 238000011069 regeneration method Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 4
- 238000010926 purge Methods 0.000 description 3
- 230000003213 activating effect Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Abstract
Molecular sieve drying tower relates to the drying tower that a dry liquid material used. Mainly for solving nitrogen gas and the big problem design of electrical loss volume when at present carrying out activation regeneration to the molecular sieve. It includes the tower body, and there is the import of hot nitrogen gas at the tower body top, and there are nitrogen gas and water export in the tower body bottom, is equipped with upper junction plate and lower connecting plate in the tower body, still includes a plurality of tubulation, each tubulation upper portion all fix on the upper junction plate, the lower part of each tubulation is all fixed under on the connecting plate, upper junction plate and connecting plate down all are equipped with the opening corresponding tubulation department, the upper junction plate with establish steam inlet and steam outlet on the tower body between the connecting plate down, the molecular sieve all is equipped with in every tubulation, be equipped with the liquid material import on the tower body of upper junction plate top, be equipped with liquid material on the tower body below the lower connecting plate and export. The advantage is reducible half electrical heating energy consumption and nitrogen gas use amount.
Description
Technical field:
The utility model relates to the drying tower of a kind of dry liquid material.
Background technology:
When liquid material is dried in molecular sieve drying tower, the moisture that molecular sieve absorbs in liquid material reaches saturation state, when losing water separation capability, is emptied by material.Then purge molecular sieve with the hot nitrogen of 300 DEG C, carry out activating and regenerating, reuse.Being all electricity consumption heated nitrogen when at present molecular sieve being carried out activating and regenerating, the waste of nitrogen and electricity is big, not only wastes the energy but also increase production cost.
Summary of the invention:
Technical problem to be solved in the utility model is to provide a kind of nitrogen and electrical loss amount is little, saves the molecular sieve drying tower of the energy.
Above-mentioned purpose is achieved in that it includes tower body, hot nitrogen import is arranged at tower body top, nitrogen and water out is had bottom tower body, it is characterized in that: in tower body, be provided with upper junction plate and lower connecting plate, also include several tubulations, described each tubulation top is all fixed on upper junction plate, the bottom of each tubulation is all fixed on lower connecting plate, upper junction plate and lower connecting plate are designed with opening at corresponding tubulation, steam inlet and steam (vapor) outlet is set on tower body between upper junction plate and lower connecting plate, it is equipped with molecular sieve in each tubulation, tower body above upper junction plate is provided with liquid material import, tower body below lower connecting plate is provided with liquid material outlet.
The utility model has the advantages that: owing to molecular sieve is contained in tubulation, liquid material liquid material import from tower body enters in each tubulation, the moisture that molecular sieve absorbs in material reaches saturation state, when losing water separation capability, material is emptied, connect up the tower body shell between plate and lower connecting plate from steam inlet and be passed through the steam of 150 DEG C, molecular sieve is preheated, when molecular sieve temperature reaches more than 100 DEG C, in molecular sieve, it is passed through heated dry air pre-purge, dry residual materials, be passed through hot nitrogen the most again and purge, reach drying effect.It can reduce half electrical heating energy consumption and nitrogen usage amount, improves efficiency, alleviates machine utilization, reduces cost.
Accompanying drawing illustrates:
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention:
With reference to Fig. 1, it includes tower body 1, hot nitrogen import 2 is arranged at tower body top, nitrogen and water out 3 is had bottom tower body, it is characterized in that: in tower body, be provided with upper junction plate 4 and lower connecting plate 5, also include several tubulations 6, described each tubulation top is all fixed on upper junction plate, the bottom of each tubulation is all fixed on lower connecting plate, upper junction plate and lower connecting plate are designed with opening at corresponding tubulation, steam inlet 7 and steam (vapor) outlet 8 is set on tower body between upper junction plate and lower connecting plate, molecular sieve 9 it is equipped with in each tubulation, tower body above upper junction plate is provided with liquid material import 10, tower body below lower connecting plate is provided with liquid material outlet 11.
Claims (1)
1. molecular sieve drying tower, including tower body (1), hot nitrogen import (2) is arranged at tower body top, nitrogen and water out (3) is had bottom tower body, it is characterized in that: in tower body, be provided with upper junction plate (4) and lower connecting plate (5), also include several tubulations (6), described each tubulation top is all fixed on upper junction plate, the bottom of each tubulation is all fixed on lower connecting plate, upper junction plate and lower connecting plate are designed with opening at corresponding tubulation, steam inlet (7) and steam (vapor) outlet (8) is set on tower body between upper junction plate and lower connecting plate, molecular sieve (9) it is equipped with in each tubulation, tower body above upper junction plate is provided with liquid material import (10), tower body below lower connecting plate is provided with liquid material outlet (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620063781.3U CN205516623U (en) | 2016-01-24 | 2016-01-24 | Molecular sieve drying tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620063781.3U CN205516623U (en) | 2016-01-24 | 2016-01-24 | Molecular sieve drying tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205516623U true CN205516623U (en) | 2016-08-31 |
Family
ID=56768646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620063781.3U Expired - Fee Related CN205516623U (en) | 2016-01-24 | 2016-01-24 | Molecular sieve drying tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205516623U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107586578A (en) * | 2017-09-30 | 2018-01-16 | 南京宏博环保实业有限公司 | A kind of mole sieve drier |
| CN112587958A (en) * | 2020-10-15 | 2021-04-02 | 江苏达诺尔科技股份有限公司 | Liquid or gas material dehydration pipe and dehydration device thereof |
-
2016
- 2016-01-24 CN CN201620063781.3U patent/CN205516623U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107586578A (en) * | 2017-09-30 | 2018-01-16 | 南京宏博环保实业有限公司 | A kind of mole sieve drier |
| CN112587958A (en) * | 2020-10-15 | 2021-04-02 | 江苏达诺尔科技股份有限公司 | Liquid or gas material dehydration pipe and dehydration device thereof |
| CN112587958B (en) * | 2020-10-15 | 2022-07-01 | 江苏达诺尔科技股份有限公司 | Liquid or gas material dehydration pipe and dehydration device thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 |