CN205347449U - Heat energy equipment of recycling - Google Patents
Heat energy equipment of recycling Download PDFInfo
- Publication number
- CN205347449U CN205347449U CN201520955164.XU CN201520955164U CN205347449U CN 205347449 U CN205347449 U CN 205347449U CN 201520955164 U CN201520955164 U CN 201520955164U CN 205347449 U CN205347449 U CN 205347449U
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- CN
- China
- Prior art keywords
- hot
- ion exchange
- thermokalite
- exchange system
- water cylinder
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- Expired - Fee Related
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- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model relates to a heat energy equipment of recycling locates the condensate pipe low reaches of multiple effect evaporation concentrator, including the ion exchange system, be located the ion exchange system upper reaches and provide the thermokalite jar of thermokalite to the ion exchange system to and lie in the thermokalite jar upper reaches and provide hydrothermal first hot -water cylinder to the thermokalite jar, still including lieing in a plate heat exchanger in ion exchange system low reaches and lieing in the second hot -water cylinder at the ion exchange system upper reaches, second hot -water cylinder upper end links to each other with the condensate pipe of multiple effect evaporation concentrator. The utility model discloses a heat energy equipment of recycling can effectively utilize produced heat energy in the workshop section, for BS regeneration of ionexchange resin provides proper amount heat energy, saves steam and water resource, reduction in production cost.
Description
Technical field
This utility model relates to high fructose syrup production process, particularly to a kind of heat energy recycling equipment.
Background technology
In high fructose syrup production process, most of workshop sections are desirable that the temperature of sugar liquid is all more than 60 DEG C, therefore in process of production, part workshop section is had to need to heat up, also having part workshop section can produce a certain amount of hot water, before owing to improving, this part hot water is simply merely placed in a storage tank, treat that its natural cooling is discharged again, the waste of certain heat energy can be caused.The hot water wherein produced in You Liangge workshop section is more, after multiple-effect evaporation concentrator, producing a lot of steam condensate (SC), this partial condensation coolant-temperature gage reaches 60-65 DEG C, additionally, needing hot water temperature higher during BS ion exchange system resin regeneration, for 85-90 DEG C, and the waste water having heat after regenerating produces, temperature reaches 70 DEG C～75 DEG C, therefore condensed water and this two-part hot water fiducial value of thermal wastewater of producing in the first two operation must utilize, if directly discharging or setting aside, are very unfortunate.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of heat energy recycling equipment, can effectively utilize the heat energy in workshop section, save steam.
For solving the problems referred to above, this utility model provides a kind of heat energy recycling equipment, a kind of heat energy recycling equipment, it is located at the condensate pipe downstream of multiple-effect evaporation concentrator, including ion exchange system, it is positioned at ion exchange system upstream and the thermokalite tank of thermokalite is provided to ion exchange system, and be positioned at thermokalite tank upstream and the first hot-water cylinder of hot water is provided to thermokalite tank, also include the first plate type heat exchanger being positioned at ion exchange system downstream and the second hot-water cylinder being positioned at ion exchange system upstream, second hot-water cylinder upper end is connected with the condensate pipe of multiple-effect evaporation concentrator.
Further, its second plate type heat exchanger also including being positioned between the first hot-water cylinder and ion exchange system of described heat energy recycling equipment and be positioned at the three-plate type heat exchanger between thermokalite tank and ion exchange system.
Further, described thermokalite tank, the first hot-water cylinder, the second hot-water cylinder, the second plate type heat exchanger and three-plate type heat exchanger are respectively equipped with the first steam inlet, the second steam inlet, the 3rd steam inlet, the 4th steam inlet and the 5th steam inlet；Described first plate type heat exchanger is provided with tap water inlets.
Further, described first plate type heat exchanger is provided with the first row mouth of a river that is corresponding with tap water inlets and that be connected with the first hot-water cylinder upper end；Described second plate type heat exchanger is provided with the second row mouth of a river that is corresponding with the 3rd steam inlet and that be connected with the second hot-water cylinder upper end；Described three-plate type heat exchanger is provided with the 3rd discharge outlet that is corresponding with the 5th steam inlet and that be connected with the second hot-water cylinder upper end.
Further, described first hot-water cylinder, the second hot-water cylinder and thermokalite tank lower end are respectively equipped with the first compression pump, the second compression pump and the 3rd compression pump.
The beneficial effects of the utility model:
This utility model provides a kind of heat energy recycling equipment, and it can effectively utilize produced heat energy in workshop section, provides appropriate heat energy for BS regeneration of ion-exchange resin, saves steam and water resource, reduces production cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model heat energy recycling equipment.
Detailed description of the invention:
Embodiment: as it is shown in figure 1, this utility model provides a kind of heat energy recycling equipment, it is adaptable to the hot water of 60-65 DEG C produced after steam condensation in multiple-effect evaporation concentration section is again for BS regeneration of ion-exchange resin.This heat energy recycling equipment is positioned at the downstream of multiple-effect evaporation concentrator (not shown), and nucleus equipment is BS ion exchange system 1.BS ion exchange system 1 upstream is provided with thermokalite tank 2, thermokalite tank 2 has the alkali liquor of higher concentration, need to use hot water that alkali liquor is diluted to low concentration in use and can be only used for BS regeneration of ion-exchange resin, therefore it is provided with the first hot-water cylinder 3 in the upstream of thermokalite tank 2 and provides hot water for it, simultaneously, thermokalite tank 2 lower end is provided with the first steam inlet 21, for alkali liquor is heated up.The thermal wastewater of 70-75 DEG C can be produced after BS ion exchange system 1 regenerates, thermal wastewater is also effectively utilized by this heat energy recycling equipment, namely the first plate type heat exchanger 4 is set at the floss hole 11 of BS ion exchange system 1, waste water enters the first plate type heat exchanger 4 by the first entrance 41, another runner of first plate type heat exchanger 4 is provided with tap water inlets 42, the tap water heating of room temperature can be become the hot water of uniform temperature, the first row mouth of a river 43 of tap water inlets 42 correspondence is connected with the first hot-water cylinder 3 upper end, sends into the first hot-water cylinder 3 by the hot water after heating and is stored.First plate type heat exchanger 4 is additionally provided with the wastewater outlet 44 corresponding with the first entrance 41, and wastewater outlet 44 leads directly to sewage disposal.Simultaneously, first branch 31 in the first hot-water cylinder 3 downstream is additionally provided with the second plate type heat exchanger 5, by the second plate type heat exchanger 5, the hot water of 85-90 DEG C after heating again being sent into BS ion exchange system 1, therefore another runner of the second plate type heat exchanger 5 is provided with the 4th steam inlet 51 and provides thermal source.It is additionally provided with the second branch 32, and it is connected with thermokalite tank 2 upper end, provides hot water for thermokalite tank 2.
This equipment is provided with multiple-effect evaporation concentrator downstream for storing the second hot-water cylinder 6 of the condensed water produced in multiple-effect evaporation concentration section, is provided with the condensing water inlet 61 accessing condensed water, and the second hot-water cylinder 6 downstream is BS ion exchange system.Meanwhile, in the second plate type heat exchanger 5, the second row mouth of a river 52 corresponding with the 4th steam inlet 51 and this second hot-water cylinder 6 upper end connect, and are imported by the condensed water of its generation in the second hot-water cylinder 6 and are stored.Hot water owing to storing in the first hot-water cylinder 3 and the second hot-water cylinder 6 can not reach the requirement of 85-90 DEG C needed for BS ion exchange system 1, therefore also need to be respectively provided with the second steam inlet 62, steam inlet the 33, the 3rd at the first hot-water cylinder 3 and the second hot-water cylinder 6 lower end, for the heating again of hot water.The outlet of aforementioned thermokalite tank 2 is provided with three branches, and the 3rd branch 22 is the circulating line being connected with thermokalite tank 2 upper end, when hot paper mill wastewater does not meet BS ion exchange resin regeneration desired concn, alkali liquor imports thermokalite tank 2 again and is adjusted；4th branch 23 is directly connected with BS ion exchange system 1, and when the Pressure, Concentration, Temperature of thermokalite all meets the requirements, thermokalite is introduced directly into BS ion exchange system 1 by the 4th branch 23；Quintafurcation 24 is to be connected with BS ion exchange system 1 by three-plate type heat exchanger 7, when the temperature of thermokalite is too low, then needs to be again heated to by thermokalite temperature required through three-plate type heat exchanger 7.Therefore this another runner of three-plate type heat exchanger 7 is provided with the 5th steam inlet 71, same, and the 3rd discharge outlet 72 corresponding with the 5th steam inlet 71 is connected with the second hot-water cylinder 6 upper end, is imported by the condensed water of its generation in the second hot-water cylinder 6 and is stored.Simultaneously for the ease of the liquid in each storage tank is squeezed into next equipment, it is respectively equipped with the first compression pump the 8, second compression pump 9 and the 3rd compression pump 10 at thermokalite the 2, first hot-water cylinder 3 and the second hot-water cylinder 6 lower end.
The above is preferred implementation of the present utility model; it should be pointed out that, for those skilled in the art, under the premise without departing from this utility model principle; can also making some improvements and modifications, these improvements and modifications are also considered as protection domain of the present utility model.
Claims (5)
1. a heat energy recycling equipment, it is located at the condensate pipe downstream of multiple-effect evaporation concentrator, including ion exchange system, it is positioned at ion exchange system upstream and the thermokalite tank of thermokalite is provided to ion exchange system, and be positioned at thermokalite tank upstream and the first hot-water cylinder of hot water is provided to thermokalite tank, it is characterized in that, also including the first plate type heat exchanger being positioned at ion exchange system downstream and the second hot-water cylinder being positioned at ion exchange system upstream, the second hot-water cylinder upper end is connected with the condensate pipe of multiple-effect evaporation concentrator.
2. heat energy according to claim 1 recycling equipment, is characterized by: its second plate type heat exchanger also including being positioned between the first hot-water cylinder and ion exchange system and be positioned at the three-plate type heat exchanger between thermokalite tank and ion exchange system.
3. heat energy according to claim 1 recycling equipment, is characterized by: described thermokalite tank, the first hot-water cylinder, the second hot-water cylinder, the second plate type heat exchanger and three-plate type heat exchanger are respectively equipped with the first steam inlet, the second steam inlet, the 3rd steam inlet, the 4th steam inlet and the 5th steam inlet；Described first plate type heat exchanger is provided with tap water inlets.
4. heat energy according to claim 2 recycling equipment, is characterized by: described first plate type heat exchanger is provided with the first row mouth of a river that is corresponding with tap water inlets and that be connected with the first hot-water cylinder upper end；Described second plate type heat exchanger is provided with the second row mouth of a river that is corresponding with the 3rd steam inlet and that be connected with the second hot-water cylinder upper end；Described three-plate type heat exchanger is provided with the 3rd discharge outlet that is corresponding with the 5th steam inlet and that be connected with the second hot-water cylinder upper end.
5. heat energy according to claim 1 recycling equipment, is characterized by: described first hot-water cylinder, the second hot-water cylinder and thermokalite tank lower end are respectively equipped with the first compression pump, the second compression pump and the 3rd compression pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520955164.XU CN205347449U (en) | 2015-11-26 | 2015-11-26 | Heat energy equipment of recycling |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520955164.XU CN205347449U (en) | 2015-11-26 | 2015-11-26 | Heat energy equipment of recycling |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205347449U true CN205347449U (en) | 2016-06-29 |
Family
ID=56167622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520955164.XU Expired - Fee Related CN205347449U (en) | 2015-11-26 | 2015-11-26 | Heat energy equipment of recycling |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205347449U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111544908A (en) * | 2019-02-12 | 2020-08-18 | 义铠科技股份有限公司 | Energy-saving concentration system |
-
2015
- 2015-11-26 CN CN201520955164.XU patent/CN205347449U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111544908A (en) * | 2019-02-12 | 2020-08-18 | 义铠科技股份有限公司 | Energy-saving concentration system |
| CN111544908B (en) * | 2019-02-12 | 2022-03-04 | 义铠科技股份有限公司 | Energy-saving concentration system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200806 Address after: Group 16, xintuan neighborhood committee, Dongtai town, Dongtai City, Yancheng City, Jiangsu Province Patentee after: Dongtai Pinqing Biotechnology Co., Ltd Address before: 215314, No. 530 North Qingyang Road, Zhou Town, Suzhou City, Jiangsu, Kunshan Patentee before: KUNSHAN PINQING BIOTECHNOLOGY Co.,Ltd. |
|
| 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: 20160629 Termination date: 20191126 |