CN203980248U - Reclamation of condensate water use device in Modified Starch Production - Google Patents
Reclamation of condensate water use device in Modified Starch Production Download PDFInfo
- Publication number
- CN203980248U CN203980248U CN201420250846.6U CN201420250846U CN203980248U CN 203980248 U CN203980248 U CN 203980248U CN 201420250846 U CN201420250846 U CN 201420250846U CN 203980248 U CN203980248 U CN 203980248U
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- CN
- China
- Prior art keywords
- chemicals
- communicated
- steam
- reclamation
- condensed water
- 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
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Abstract
The utility model relates to the reclamation of condensate water use device in a kind of Modified Starch Production, comprise chemicals tempering tank, the bottom of described chemicals tempering tank connects chemicals meter, the exit of described chemicals tempering tank, chemicals meter is equipped with valve, the outlet of described chemicals meter is communicated with the entrance of gas generator, the admission pipeline communication of the outlet of gas generator and reactor.The utility model sprays into reactor after liquid chemicals is converted into steam state again, raw material is mixed more even with chemicals, reacts more complete, has saved the consumption of chemicals and raw material, improves reaction efficiency, guarantees product inherent quality, increases economic efficiency.
Description
Technical field
The utility model belongs to the structural design in converted starch production technology, specifically, relates to the reclamation of condensate water use device in a kind of Modified Starch Production.
Background technology
Converted starch is a kind of starch through modification, and this kind of starch has some special physicochemical properties, can make after adding in food formula food in processing or when edible, have better performance.The production of converted starch, is that starch material and chemicals are put in vacuum reaction still, under heating condition, reacts.In prior art, mode of heating is generally the steam that adopts steam boiler to produce and heats.In steam boiler, steam out, after minute drum shunting, is sent into the gas utilization unit of each branch road through steam conveying pipe, and the condensed water in gas utilization unit is outer row directly, has wasted heat energy and water for industrial use.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, adapts to real needs, and the use device of the reclamation of condensate water in a kind of Modified Starch Production is provided.
In order to realize the purpose of this utility model, the technical solution adopted in the utility model is:
Reclamation of condensate water use device in a kind of Modified Starch Production, comprise a steam boiler, the steam that described steam boiler produces is sent into the gas utilization unit of each branch road by steam conveying pipe, the venthole of described steam boiler is connected to a minute drum, also comprise a condensed water recovery tube, the outlet of described gas utilization unit is provided with gate valve, gate valve below is connected with drain valve, the delivery port of described each drain valve is communicated with described condensed water recovery tube, each drain valve is as the branch road of condensed water recovery tube, the end of described condensed water recovery tube is communicated with the entrance of steam boiler.
The end of described condensed water recovery tube is communicated with the entrance of softened water tank, and the outlet of softened water tank is connected with deoxygenation case, and described deoxygenation case is communicated with the entrance of steam boiler.
Described gas utilization unit is also parallel with flash tank outward, and described flash tank is provided with an arm and is communicated with the outlet of each gas utilization unit.
The beneficial effects of the utility model are:
1. the heat of pair steam condensate (SC) and the water yield are carried out recycling, save boiler oil;
2. save water for industrial use, condensed water generally can, directly as boiler feedwater, can significantly reduce water for industrial use.Water after treatment still can effectively utilize;
3. save boiler feedwater disposal cost, because condensed water can be directly used in boiler feedwater, therefore can save this part water correction disposal cost;
4. the minimizing because of fuel combustion amount can alleviate atmosphere pollution, and the recovery of heat can reduce the fuel consumption of boiler, has also just reduced the discharge capacity of flue dust and sulfur dioxide; Meanwhile, eliminate the hot gas producing because of discharge condensed water, improved working environment;
5. improve boiler BTHE, due to the utilization of condensed water, make boiler feed temperature increase, fuel saving, improves boiler BTHE, has given full play to the potentiality of boiler.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, 1 is steam boiler, and 2 is steam conveying pipe, and 3 is gas utilization unit, 4 minutes drums, and 5 is condensed water recovery tube, and 6 is gate valve, and 7 is drain valve, and 8 is softened water tank, and 9 for deoxygenation case, and 10 is flash tank, 101 arms that are flash tank.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Embodiment: referring to Fig. 1.
Reclamation of condensate water use device in a kind of Modified Starch Production, comprise a steam boiler 1, the steam that described steam boiler 1 produces is sent into the gas utilization unit 3 of each branch road by steam conveying pipe 2, the venthole of described steam boiler 1 is connected to a minute drum 4, also comprise a condensed water recovery tube 5, the outlet of described gas utilization unit 3 is provided with gate valve 6, gate valve 6 belows are connected with drain valve 7, the delivery port of described each drain valve 7 is communicated with described condensed water recovery tube 5, each drain valve 7 is as the branch road of condensed water recovery tube 5, the end of described condensed water recovery tube 5 is communicated with the entrance of steam boiler 1.
The end of described condensed water recovery tube is communicated with the entrance of softened water tank 8, and the outlet of softened water tank 8 is connected with deoxygenation case 9, and described deoxygenation case 9 is communicated with the entrance of steam boiler 1.
The steam that steam boiler 1 produces, through 4 shuntings of minute drum, send into the gas utilization unit 3 of each branch road, the outlet of gas utilization unit 3 is provided with gate valve 6, gate valve 6 belows are provided with drain valve 7, drain valve 7 is draining resistance vapour effectively, when getting rid of the condensate water of gas utilization unit generation rapidly, prevent steam leakage, condensate water collects in condensed water recovery tube 5 after discharging via drain valve 7, entering softened water tank 8 condensed waters is softened, then, after 9 deoxygenations of deoxygenation case, again enter steam boiler 1, heating generates steam and continues to be fed into steam conveying pipe 2.
Described gas utilization unit 3 is outer is also parallel with flash tank 10, and described flash tank 10 is provided with an arm 101 and is communicated with the outlet of each gas utilization unit 3.Part flash steam is sent into each gas utilization unit by flash tank 10 and is utilized for 3 two times.
The utility model carries out recycling to the heat of steam condensate (SC) and the water yield, saves boiler oil, saves water for industrial use, save boiler feedwater disposal cost, alleviate atmosphere pollution, improved working environment, make boiler BTHE improve simultaneously, given full play to the potentiality of boiler.
Claims (3)
1. the reclamation of condensate water use device in a Modified Starch Production, comprise a steam boiler (1), the steam that described steam boiler (1) produces is sent into the gas utilization unit (3) of each branch road by steam conveying pipe (2), the venthole of described steam boiler (1) is connected to a minute drum (4), it is characterized in that: also comprise a condensed water recovery tube (5), the outlet of described gas utilization unit (3) is provided with gate valve (6), gate valve (6) below is connected with drain valve (7), the delivery port of described each drain valve (7) is communicated with described condensed water recovery tube (5), each drain valve (7) is as the branch road of condensed water recovery tube (5), the end of described condensed water recovery tube (5) is communicated with the entrance of steam boiler (1).
2. the reclamation of condensate water use device in Modified Starch Production according to claim 1, it is characterized in that: the end of described condensed water recovery tube (5) is communicated with the entrance of softened water tank (8), the outlet of softened water tank (8) is connected with deoxygenation case (9), and described deoxygenation case (9) is communicated with the entrance of steam boiler (1).
3. the reclamation of condensate water use device in Modified Starch Production according to claim 2, it is characterized in that: described gas utilization unit (3) is outer is also parallel with flash tank (10), and described flash tank (10) is provided with an arm (101) and is communicated with the outlet of each gas utilization unit (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420250846.6U CN203980248U (en) | 2014-05-16 | 2014-05-16 | Reclamation of condensate water use device in Modified Starch Production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420250846.6U CN203980248U (en) | 2014-05-16 | 2014-05-16 | Reclamation of condensate water use device in Modified Starch Production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203980248U true CN203980248U (en) | 2014-12-03 |
Family
ID=51977682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420250846.6U Expired - Fee Related CN203980248U (en) | 2014-05-16 | 2014-05-16 | Reclamation of condensate water use device in Modified Starch Production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203980248U (en) |
-
2014
- 2014-05-16 CN CN201420250846.6U patent/CN203980248U/en not_active Expired - Fee Related
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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 |
Granted publication date: 20141203 Termination date: 20150516 |
|
| EXPY | Termination of patent right or utility model |