CN207614810U - saponification tower assembly - Google Patents
saponification tower assembly Download PDFInfo
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- CN207614810U CN207614810U CN201721452606.4U CN201721452606U CN207614810U CN 207614810 U CN207614810 U CN 207614810U CN 201721452606 U CN201721452606 U CN 201721452606U CN 207614810 U CN207614810 U CN 207614810U
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- saponification
- steam
- column
- storage tank
- pipe
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Abstract
The utility model is related to saponification technical equipment, disclose a kind of saponification tower assembly, storage tank including saponification column, for storing steam condensate (SC), saponification tower side wall is equipped with steam port, the first pipe for the raw steam that circulates is connected on steam port, storage tank is equipped with inlet and outlet, and the outlet on storage tank is connected with the second pipe for flowing steam condensed water, second pipe is communicated with first pipe, and the import on storage tank is connected with the third pipeline for the condensed water that circulates.The utility model is incorporated with before raw steam enters saponification column and flashes off 105 ° of saturated vapor under condition of negative pressure by the steam condensate (SC) of 0.8MPa, it is that saponification column is heated together, equally making the control of saponification kettle temperature degree, this structure can save 0.5 0.8 tons of raw steam per hour under conditions of between 85 ° 95 °.
Description
Technical field
The utility model is related to saponification technical equipment, more particularly to a kind of saponification tower assembly.
Background technology
Currently, being directly to lead into saponification column progress using raw steam in saponification technical field, when saponification column heats
Heating, on an hourly basis 1.25 tons of steam/ton epoxy calculate, 20Kt/a yield requires 3.5 tons of life steam and enters per hour
In saponification column（It is calculated within 24 hours by annual production production daily in 300 days, 20Kt/a（Produce 20 kilotons per year）Epoxy yield is converted into per small
When produce 2.78 tons of epoxies, 2.78*1.25=3.5）.In addition giving birth to steam cannot adequately use, and energy consumption is big.In material exist compared with
, easily there is foaming phenomena in multiple component, seriously affects the stable operation of whole system.
Invention content
For the utility model for the larger disadvantage of steam usage amount is given birth in the prior art, raw steam can be reduced by providing one kind
The saponification tower assembly of usage amount.
In order to solve the above-mentioned technical problem, the utility model is addressed by following technical proposals：
Saponification tower assembly, including saponification column, the storage tank for storing steam condensate (SC), saponification tower side wall are equipped with steam
Mouthful, the first pipe for the raw steam that circulates is connected on steam port, storage tank is equipped with inlet and outlet, and the outlet on storage tank connects
It is connected to the second pipe for flowing steam condensed water, second pipe is communicated with first pipe, and the import connection on storage tank is useful
In the third pipeline of circulation condensed water.
Preferably, being equipped with gas outlet at the top of saponification column, saponification tower bottom is exported equipped with saponification Liquid Residue.
Preferably, saponification column is internally provided with spiral helicine jet chimney, jet chimney one end is connected with steam port.
Preferably, jet chimney is equipped with plurality of holes, hole is distributed on jet chimney.
Preferably, saponification column internal upper part is equipped with wire mesh demister, wire mesh demister outer rim is fixed on saponification inner wall of tower
Together.
Preferably, saponification tower side wall is equipped with feed inlet, it is located in saponification column mutual equipped with plural block below feed inlet
Staggered sieve plate.
The utility model has significant technique effect as a result of above technical scheme：Enter saponification in raw steam
Be incorporated with before tower and flash off 105 ° of saturated vapor under condition of negative pressure by the steam condensate (SC) of 0.8MPa, together for saponification column into
Row heating, equally making the control of saponification kettle temperature degree, this structure can save raw steam per hour under conditions of between 85 ° -95 °
It 0.5-0.8 tons, is calculated according to producing in year 7200 hours, whole year can save raw steam 3600-5760 tons；It is provided with the steaming of helical axis
Steam pipe road, it can be ensured that raw steam is uniformly distributed, and is improved coming into full contact with for raw steam and material, is improved the utilization rate of raw steam,
Save resource；Wire mesh demister is set, for abolishing the foam in saponification column, prevents the stable operation of blistering influence system.
Description of the drawings
Fig. 1 is the easy structure figure of the utility model embodiment 1.
Fig. 2 is the easy structure figure of the saponification column of the utility model embodiment 1.
Fig. 3 is the part amplification assumption diagram of the saponification column of Fig. 2.
The toponym that each number designation is referred in attached drawing is as follows：Wherein 1-saponification column, 2-storage tanks, the 3-the first pipe
Road, 4-second pipes, 5-third pipelines, 6-feed inlets, 7-steam ports, 8-gas outlets, 9-saponification Liquid Residues outlet,
10-jet chimneys, 11-holes, 12-wire mesh demisters, 13-feed pipes, 14-sieve plates.
Specific implementation mode
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings.
Embodiment 1
Saponification tower assembly, as shown in Figure 1, including saponification column 1, the storage tank 2 for storing steam condensate (SC), 1 side of saponification column
Wall lower part is equipped with steam port 7, is connected with the first pipe 3 for the raw steam that circulates on steam port 7, storage tank 2 be equipped with import and
It exports, the outlet on storage tank 2 is connected with the second pipe 4 for flowing steam condensed water, second pipe 4 and 3 phase of first pipe
Logical, the import on storage tank 2 is connected with the third pipeline 5 for the condensed water that circulates.1 top of saponification column is equipped with gas outlet 8, saponification column
1 bottom is equipped with saponification Liquid Residue and exports 9.The pump for pumping is connected on gas outlet 8.
Operation principle：Condensed water forms the steam condensate (SC) with 0.8MPa, the storage tank 2 under condition of negative pressure in storage tank 2
Top flashes off 105 ° of saturated vapor and is successively entered in first pipe 3 by second pipe 4, into first pipe 3
Saturated vapor is incorporated to life steam of the circulation in first pipe 3, and the two together heats saponification kettle into saponification column 1, and
The prior art is compared, and is equally to control the temperature of saponification kettle between 85 ° -95 °, the saponification tower assembly of the application per hour may be used
Raw 0.5-0.8 tons of steam is saved, is calculated according to producing in year 7200 hours, whole year can save raw steam 3600-5760 tons.
Embodiment 2
As shown in Figure 2 to Figure 3, basic structure is same as Example 1, the difference is that saponification column 1 is internally provided with steaming
Steam pipe road 10.1 side wall upper part of saponification column is equipped with feed inlet 6, and 10 one end of jet chimney is connected with steam port 7, and jet chimney 10 is another
One end is located at 7 top of steam port.Jet chimney 10 is equipped with plurality of holes 11, and hole 11 is distributed on jet chimney 10, raw steam
Through when via 11 can part through hole 11 enter inside saponification column 1, for saponification.Jet chimney 10 is helical form, can be true
Being uniformly distributed for raw steam is protected, coming into full contact with for raw steam and material is improved, improves the utilization rate of raw steam, save resource.
1 internal upper part of saponification column is equipped with wire mesh demister 12, and 12 outer rim of wire mesh demister is welded on one with 1 inner wall of saponification column
It rises, wire mesh demister 12 is arranged above feed inlet 6.Wire mesh demister 12 is used to abolish the foam in saponification column 1, prevents from blistering
The stable operation of influence system.
Feed pipe 13 is connected on feed inlet 6, the axis and 1 inner wall of saponification column of feed inlet 6 are tangent, position in saponification column 1
In being installed with eddy flow baffle plate in 6 entry wall of feed inlet, by the way of tangential feed, feed pipe 13 and saponification column 1
Inner wall tangentially can extend disengaging time, be more advantageous in gas from liquid and escape after installing eddy flow baffle plate.
It is installed with vortex breaker at saponification Liquid Residue outlet 9, can prevent from out taking away the gas in saponification column 1 when liquid.
It is equipped with the sieve plate 14 that plural block is intertwined positioned at 6 lower section of feed inlet in saponification column 1, the inclination of sieve plate 14 is set
It sets, it can be ensured that the liquid rested on sieve plate 14 can flow to 1 lower part of saponification column under self gravitation effect.In the present embodiment
In, the sieve plate 14 in left side is seven pieces and interval is arranged, and the sieve plate 14 on right side is seven pieces and interval setting, sieve plate 14 and the right side in left side
The sieve plate 14 of side interlocks.Material becomes superheated liquid and hastily partial gasification, unvaporized liquid after entering in saponification column 1
Under the effect of gravity, contacted on sieve plate 14 with the life steam risen through sieve plate 14, to make vehicle repair major more come into full contact with and
Separation.Sieve plate 14 is semicircle, and there is overlapping in only its end in orthographic projection between adjacent upper layer and lower layer sieve plate 14.
Sieve plate 14 is equipped with a plurality of sieve pores, and the diameter of sieve pore is between 20-25mm, and sieve pore is uniformly distributed on sieve plate 14, phase
The number for the sieve pore opened on the sieve plate 14 on adjacent two layers of sieve plate, 14 its upper layer is less than the number of the sieve plate 14 of lower layer.The setting of sieve pore
Convenient for the rising of raw steam, and increase the travel time of raw steam, extends the working time of raw steam, improve the utilization of the energy
Rate.
In short, the above is only the preferred embodiment of the present invention, it is all according to present utility model application the scope of the claims institute
The equivalent changes and modifications of work should all belong to the covering scope of the utility model patent.
Claims (6)
1. saponification tower assembly, including saponification column（1）, saponification column（1）Side wall is equipped with steam port（7）, steam port（7）On be connected with
First pipe for the raw steam that circulates（3）, it is characterised in that：It further include the storage tank for storing steam condensate (SC)（2）, storage tank
（2）It is equipped with inlet and outlet, storage tank（2）On outlet be connected with the second pipe for flowing steam condensed water（4）, second
Pipeline（4）With first pipe（3）It communicates, storage tank（2）On import be connected with the third pipeline for the condensed water that circulates（5）.
2. saponification tower assembly according to claim 1, it is characterised in that：Saponification column（1）Top is equipped with gas outlet（8）, soap
Change tower（1）Bottom is exported equipped with saponification Liquid Residue（9）.
3. saponification tower assembly according to claim 1, it is characterised in that：Saponification column（1）It is internally provided with spiral helicine steam
Pipeline（10）, jet chimney（10）One end and steam port（7）It is connected.
4. saponification tower assembly according to claim 3, it is characterised in that：Jet chimney（10）It is equipped with plurality of holes
（11）, hole（11）It is distributed on jet chimney（10）On.
5. saponification tower assembly according to claim 1, it is characterised in that：Saponification column（1）Internal upper part is equipped with wire mesh demister
（12）, wire mesh demister（12）Outer rim and saponification column（1）Inner wall is fixed together.
6. saponification tower assembly according to claim 1, it is characterised in that：Saponification column（1）Side wall is equipped with feed inlet（6）,
Saponification column（1）It is interior to be located at feed inlet（6）Lower section is equipped with the sieve plate that plural block is intertwined（14）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721452606.4U CN207614810U (en) | 2017-11-03 | 2017-11-03 | saponification tower assembly |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721452606.4U CN207614810U (en) | 2017-11-03 | 2017-11-03 | saponification tower assembly |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207614810U true CN207614810U (en) | 2018-07-17 |
Family
ID=62827225
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721452606.4U Active CN207614810U (en) | 2017-11-03 | 2017-11-03 | saponification tower assembly |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207614810U (en) |
-
2017
- 2017-11-03 CN CN201721452606.4U patent/CN207614810U/en active Active
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| GR01 | Patent grant |