CN203816246U - Special triple-effect evaporation system for polyester production enterprises - Google Patents
Special triple-effect evaporation system for polyester production enterprises Download PDFInfo
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- CN203816246U CN203816246U CN201420182684.7U CN201420182684U CN203816246U CN 203816246 U CN203816246 U CN 203816246U CN 201420182684 U CN201420182684 U CN 201420182684U CN 203816246 U CN203816246 U CN 203816246U
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Abstract
The utility model discloses a special triple-effect evaporation system for polyester production enterprises. The triple-effect evaporation system comprises a master steam supply pipe, a liquid inlet pipe and a triple-effect evaporator. The triple-effect evaporation system is characterized by also comprising a heat exchanger, an intermediate tank and a steam jetting pump, wherein the liquid inlet pipe is communicated with a material inlet through the heat exchanger; steam outlets of a first steam jacket and a second steam jacket are communicated with the intermediate tank through pipelines; a steam outlet of a third steam jacket is communicated with the hot source input end of the heat exchanger; the hot source output end of the heat exchanger is communicated with the intermediate tank; a condensate water outlet is formed in the bottom of the intermediate tank and a heat preserving jacket is arranged on the outer side of the intermediate tank; an inlet of the steam jetting pump is connected with the master steam supply pipe, a steam pumping hole of the steam jetting pump is connected with the intermediate tank, and a steam outlet of the steam jetting pump is connected with a steam inlet of the first steam jacket. Compared with the prior art, the triple-effect evaporation system has the advantages of high concentration efficiency, capability of effectively utilizing excess hot steam, and good energy-saving effect.
Description
Technical field
The utility model relates to a kind of polyester production facility, particularly a kind of triple effect evaporation system of production of polyester enterprise-specific.
Background technology
Polyamide fibre is again polycaprolactam fiber, and its raw materials for production are polyamide section.Polyamide section needs caprolactam solution to concentrate purification in process of production, main equipment for purifying is triple effect evaporator, triple effect evaporator is prior art, its principle is by an effect tank, two effect tanks and three evaporator series of triple effect tank get up, the indirect steam of previous stage evaporimeter becomes the heating steam of rear one-level evaporimeter, can form like this three grades concentrates, have advantages of energy-efficient, the shortcoming that this triple effect evaporator exists is: from the first steam jacket, the steam that the second steam jacket and the 3rd steam jacket steam (vapor) outlet are discharged is all directly emptying, this part steam pressure is 2.5 kilograms of left and right, containing a large amount of waste heats, drain very unfortunate, be unfavorable for energy-conservation.
Summary of the invention
The technical problem that will solve of the present utility model is: the triple effect evaporation system that a kind of more energy-conservation production of polyester enterprise-specific is provided.
The triple effect evaporation system of the production of polyester enterprise-specific that the utility model is designed, comprise steam supply house steward, feed tube and triple effect evaporator, described triple effect evaporator has an effect tank, two effect tank and triple effect tanks, in an effect tank top, be provided with charging aperture, at an effect tank, two effect tanks and triple effect tank, be respectively equipped with the first steam jacket, the second steam jacket and the 3rd steam jacket outward, the steam inlet of the second steam jacket is connected with the venthole of an effect tank top, and the steam inlet of the 3rd steam jacket is connected with the venthole of two effect tank tops; It is characterized in that also comprising heat exchanger, pans and steam jet pump, described feed tube is by described heat exchanger and described feeding inlet; The steam (vapor) outlet of described the first steam jacket and the second steam jacket communicates with described pans by pipeline; The steam (vapor) outlet of described the 3rd steam jacket communicates with the thermal source input of described heat exchanger, and the thermal source output of described heat exchanger communicates with described pans; Described intervalve bottom has condensation-water drain, outside has insulation jacket; Described steam jet pump, its import is connected with described steam supply house steward, its extraction opening is connected with pans, and its steam drain is connected with the steam inlet of the first steam jacket.
Caprolactam solution can carry out three step evaporation and concentration at an effect tank, two effect tanks, triple effect tank, and efficiency is higher; From effect tank venthole steam out, enter the second steam jacket for its heat supply, from two effect tank ventholes steam out, enter the 3rd steam jacket for its heat supply.From the second steam jacket and the 3rd steam jacket steam (vapor) outlet afterheat steam out, enter in pans and store, when passing through steam jet pump, steam supply house steward initial steam out can produce negative pressure, negative pressure can be by the afterheat steam in pans also suction to steam jet pump, both are the first steam jacket steam supply jointly after mixing also supercharging, form thus effectively circulation, steam has just obtained good recycling like this, on the other hand, the steam of discharging from the 3rd steam jacket is heat exchanger heat supply, give the process that enters the preheating of caprolactam solution between triple effect evaporator, to improve the temperature of caprolactam solution, improve thickening efficiency, from exchanger heat source output terminal steam and condensed water out, enter pans, steam can be utilized, condensed water can pass through condensation-water drain centralized collection.
The triple effect evaporation system of the production of polyester enterprise-specific that the utility model is designed, its advantage is compared with prior art: 1, thickening efficiency is high; 2, can effectively utilize afterheat steam; 3, energy-saving effect is better.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: steam supply house steward 1, feed tube 2, triple effect evaporator 3, an effect tank 31, two effect tanks 32, triple effect tank 33, steam jet pump 4, import 41, extraction opening 42, steam drain 43, the first steam jacket 5, the second steam jacket 6, the 3rd steam jacket 7, venthole 8, steam inlet 9, steam (vapor) outlet 10, charging aperture 11, heat exchanger 12, pans 13, condensation-water drain 14, insulation jacket 15, pump 16, feed liquid conveyance conduit 17, vavuum pump 18, concentrated solution outlet 19, valve 20.
The specific embodiment
Below by embodiment, the utility model will be further described by reference to the accompanying drawings.
Embodiment 1:
As shown in Figure 1, the triple effect evaporation system of the described production of polyester enterprise-specific of the present embodiment, comprise steam supply house steward 1, feed tube 2 and triple effect evaporator 3, triple effect evaporator 3 has an effect tank 31, two effect tank 32 and triple effect tanks 33, at effect tank 31 tops, be provided with charging aperture 11, at an effect tank 31, outer first steam jacket 5 that is respectively equipped with of two effect tanks 32 and triple effect tank 33, the second steam jacket 6 and the 3rd steam jacket 7, the steam inlet 9 of the second steam jacket 6 is connected with the venthole 8 at effect tank 31 tops, the steam inlet 9 of the 3rd steam jacket 7 is connected with the venthole 8 at two effect tank 32 tops, it is characterized in that also comprising heat exchanger 12, pans 13 and steam jet pump 4, feed tube 2 communicates with charging aperture 11 by heat exchanger 12, the steam (vapor) outlet 10 of the first steam jacket 5 and the second steam jacket 6 communicates with pans 13 by pipeline, the steam (vapor) outlet 10 of the 3rd steam jacket 7 communicates with the thermal source input of heat exchanger 12, and the thermal source output of heat exchanger 12 communicates with pans 13, intervalve bottom has condensation-water drain 14, outside has insulation jacket 15, and insulation jacket 15 can play heat insulation effect, prevents the steam-condensation in pans, thereby further improves utilization rate of waste heat, described steam jet pump 4, its import 41 is connected with steam supply house steward 1, its extraction opening 42 is connected with pans 13, and its steam drain 43 is connected with the steam inlet 9 of the first steam jacket 5.It should be noted that: triple effect evaporator and steam jet pump can be selected the conventional model on market, at this, do not describe in detail.The afterheat steam amount of discharging due to the second steam jacket 6, the 3rd steam jacket 7 is larger, preferably it is recycled.
The triple effect evaporation system of the described production of polyester enterprise-specific of the present embodiment, compare with existing triple effect evaporator, steam consumption can reduce 3.8%, for Reducing Cost in Enterprises is contributed, can effectively reduce in addition the high problem of workshop temperature causing because steam is in line, make workman's working environment more comfortable, this triple effect evaporation system, can in production of polyester enterprise, extensively promote, be particularly suitable for producing slices of caprone.
Claims (1)
1. the triple effect evaporation system of a production of polyester enterprise-specific, comprise steam supply house steward (1), feed tube (2) and triple effect evaporator (3), described triple effect evaporator (3) has an effect tank (31), two effect tank (32) and triple effect tanks (33), at effect tank (31) top, be provided with charging aperture (11), at an effect tank (31), outer the first steam jacket (5) that is respectively equipped with of two effect tanks (32) and triple effect tank (33), the second steam jacket (6) and the 3rd steam jacket (7), the steam inlet (9) of the second steam jacket (6) is connected with the venthole (8) at effect tank (31) top, the steam inlet (9) of the 3rd steam jacket (7) is connected with the venthole (8) at two effect tank (32) tops, it is characterized in that also comprising heat exchanger (12), pans (13) and steam jet pump (4), described feed tube (2) communicates with described charging aperture (11) by described heat exchanger (12), the steam (vapor) outlet (10) of described the first steam jacket (5) and the second steam jacket (6) communicates with described pans (13) by pipeline, the steam (vapor) outlet (10) of described the 3rd steam jacket (7) communicates with the thermal source input of described heat exchanger (12), and the thermal source output of described heat exchanger (12) communicates with described pans (13), described intervalve bottom has condensation-water drain (14), outside has insulation jacket (15), described steam jet pump (4), its import (41) is connected with described steam supply house steward (1), its extraction opening (42) is connected with pans (13), and its steam drain (43) is connected with the steam inlet (9) of the first steam jacket (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420182684.7U CN203816246U (en) | 2014-04-15 | 2014-04-15 | Special triple-effect evaporation system for polyester production enterprises |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420182684.7U CN203816246U (en) | 2014-04-15 | 2014-04-15 | Special triple-effect evaporation system for polyester production enterprises |
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| Publication Number | Publication Date |
|---|---|
| CN203816246U true CN203816246U (en) | 2014-09-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420182684.7U Expired - Fee Related CN203816246U (en) | 2014-04-15 | 2014-04-15 | Special triple-effect evaporation system for polyester production enterprises |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107596715A (en) * | 2017-11-06 | 2018-01-19 | 李少艳 | A kind of connection in series-parallel multiple-effect condensation technology |
| CN110124341A (en) * | 2019-06-20 | 2019-08-16 | 刘向东 | It is a kind of suitable for crystalline solid solid content is high and the multi-effect evaporator of the high-salt wastewater containing organic matter |
-
2014
- 2014-04-15 CN CN201420182684.7U patent/CN203816246U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107596715A (en) * | 2017-11-06 | 2018-01-19 | 李少艳 | A kind of connection in series-parallel multiple-effect condensation technology |
| CN107596715B (en) * | 2017-11-06 | 2021-06-01 | 李少艳 | Series-parallel connection multiple-effect concentration process |
| CN110124341A (en) * | 2019-06-20 | 2019-08-16 | 刘向东 | It is a kind of suitable for crystalline solid solid content is high and the multi-effect evaporator of the high-salt wastewater containing organic matter |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140910 Termination date: 20150415 |
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| EXPY | Termination of patent right or utility model |