CN205138254U - High fructose syrup production cooling system of workshop section - Google Patents
High fructose syrup production cooling system of workshop section Download PDFInfo
- Publication number
- CN205138254U CN205138254U CN201520921569.1U CN201520921569U CN205138254U CN 205138254 U CN205138254 U CN 205138254U CN 201520921569 U CN201520921569 U CN 201520921569U CN 205138254 U CN205138254 U CN 205138254U
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- China
- Prior art keywords
- cooling
- water
- workshop section
- cooling system
- cooling tower
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- Expired - Fee Related
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Abstract
The utility model relates to a high fructose syrup production cooling system of workshop section, including the indirect heating equipment that is used for cooling off high fructose syrup, be located the indirect heating equipment upper reaches and each other parallelly connected frozen water machine and cooling tower, be located the intake pump between cooling tower and the indirect heating equipment. This high fructose syrup production cooling system of workshop section utilizes effectively that the sensible heat exchanging principle can not only reduce power consumption, plant maintenance and maintenance cost with the water cooling between latent heat evaporation principle soft breeze, water, greatly reduced manufacturing cost, simultaneously, during the use as required optionally use cooling tower cooling or the cooling of frozen water machine or both to cooperate to use and cool down for high fructose syrup production workshop section cooling process has great flexibility.
Description
Technical field
The utility model relates to HFCS production field, particularly a kind of HFCS production workshop section cooling system.
Background technology
Take charge of at me and produce in HFCS technique, it is temperature required that most workshop section needs that liquid glucose is cooled to technique, if starch milk post liquefaction 95 DEG C insulation is after 2 hours, need be cooled to 60 DEG C and squeezes in saccharifying tank; 60 DEG C need be cooled to by 70 DEG C after semi-finished product are concentrated; 30 DEG C etc. are cooled to by 70 DEG C after finished product is concentrated.Be illustrated in figure 1 me and take charge of cooling system previously used, this cooling system by frozen water machine 01 and heat exchanger plate 02 and between hot water pipeline 03 and cold water pipes 04 form.The cool principle of heat exchanger plate is heat exchange, namely the liquid glucose that temperature is higher can drop to temperature required after the heat exchanger plate that excess temperature is lower, and low-temperature receiver is all produced by frozen water machine, frozen water machine be cooled through following steps: evaporation process, compression process, condensation process and expansion process.Frozen water machine is higher in most workshop sections frequency of utilization, and because of process requirements difference needs two frozen water machines.My Sigong process flow be 24 hours uninterrupted, through primary Calculation, two annual power consumptions of frozen water machine 77.76 ten thousand degree, and often need to safeguard frozen water machine, therefore the electric power using this cooling system to consume, maintenance cost, maintenance cost are very high.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of HFCS production workshop section cooling system, and it is on the basis of existing equipment, and newly-increased cooling tower, reduces electric power energy consumption greatly.
For solving the problem, the utility model provides a kind of HFCS production workshop section cooling system, comprise the heat transmission equipment for carrying out cooling HFCS, in heat transmission equipment upstream and frozen water machine parallel with one another and cooling tower, intake pump between cooling tower and heat transmission equipment.
Further, described frozen water machine is provided with the first water inlet end and the first water side.
Further, described cooling tower is arranged in unlimited tank, and cooling tower upper end is provided with the second water inlet end and tank lower end is provided with the second water side, and cooling tower inner upper end is provided with fan.
Further, described frozen water machine is at least one, and described cooling tower is at least one.
Further, described heat transmission equipment is heat exchanger plate, and described heat exchanger plate is provided with cooling water inlet, hot water outlet, hot sugared import and cold sugar outlet.
Further, described first water inlet end and the second water inlet end are respectively equipped with the first hot water pipeline and the second hot water pipeline; Described first water side and be respectively equipped with the first cold water pipes and the second cold water pipes between the second water side and the cooling water inlet of heat exchanger plate; The hot water outlet of described heat exchanger plate and be provided with the 3rd hot water pipeline between the first water inlet end and the second water inlet end.
Further, described heat transmission equipment, be provided with valve between frozen water machine and cooling tower.
Further, the refrigerating capacity of described frozen water machine is 125Kw, and energy consumption is for being 45Kw/h.
Further, the volume of described cooling tower is 500m
3, energy consumption is 18.5Kw/h.
The beneficial effects of the utility model:
The utility model provides a kind of HFCS production workshop section cooling system, it effectively to utilize between latent heat evaporation principle and wind, water Exchange of apparent heat principle by water cooling, power consumption, plant maintenance and maintenance cost can not only be reduced, greatly reduce production cost, simultaneously, can selectably use during use cooling tower cool or frozen water machine cooling or both are with the use of lowering the temperature, make HFCS production workshop section cooling process have larger flexibility.
Accompanying drawing explanation
Fig. 1 is original HFCS production workshop section cooling system.
Fig. 2 is the HFCS production workshop section cooling system after application the utility model.
Fig. 3 is the structural representation of heat exchanger plate in application the utility model.
Detailed description of the invention:
Embodiment: as shown in Fig. 2 to 3, the utility model provides a kind of HFCS production workshop section cooling system, and it for lowering the temperature to liquid glucose in process portion, to meet the working condition of subsequent processing.
HFCS production workshop section cooling system, be provided with the heat exchanger plate 1 for carrying out cooling HFCS, heat exchanger plate 1 is provided with cooling water inlet 101, hot water outlet 102, hot sugared import 103 and cold sugar outlet 104, from structure, the liquid glucose of heat enters from the sugared import 103 of heat, cold pipeline (figure has no) through heat exchanger plate 1 inside is lowered the temperature, thus the liquid glucose after cooling flows out from cold sugar outlet 104.External source enters from cooling water inlet 101, from hot water outlet 102 discharges after heating up after heat exchange.
This HFCS production workshop section cooling system also comprises the frozen water machine 2 and two cooling towers 3 that are positioned at heat exchanger plate 1 upstream, and the refrigerating capacity of frozen water machine 2 is 125Kw, and energy consumption is for being 45Kw/h, and the volume of cooling tower is 500m
3, energy consumption is 18.5Kw/h.Wherein two cooling towers 3 are parallel with one another arranges composition cooling tower group, and be all placed in a unlimited tank 4, the open system that tank 4 and space outerpace are formed is conducive to the cooling of hot water.Frozen water machine 2 and cooling tower group are connected in parallel in pipeline, can be respectively heat exchanger plate 1 and provide low-temperature receiver.Frozen water machine 2 is provided with the first water inlet end 201 and the first water side 202, and cooling tower 3 upper end is provided with the second water inlet end 301, second water inlet end 301 points of two-way and enters each cooling tower 3 respectively, and tank 4 lower end is provided with the second water side 401 and the 3rd water side 402.Cooling tower 3 inner upper end is provided with fan 302, for by the hot water in cooling tower 3 by the heat exchange of sensible heat between wind, water by water cooling, promote that hot water evaporation is taken away partial heat to lower the temperature.First water inlet end 201 and the second water inlet end 301 are respectively equipped with the first hot water pipeline 5 and the second hot water pipeline 6, for water higher for temperature is passed into frozen water machine 2 and cooling tower 3.
First water side 202 and be respectively equipped with the first cold water pipes 7 and the second cold water pipes 8 between the second water side 401 and the cooling water inlet 101 of heat exchanger plate 1, for cooled water is supplied to heat exchanger plate 1 as low-temperature receiver, wherein on the second cold water pipes 8, intake pump 9 is housed, the water that the second water side 401 is discharged can be pumped in heat exchanger plate 1.The hot water outlet of heat exchanger plate 1 and be provided with the 3rd hot water pipeline 10 between the first water inlet end 201 and the second water inlet end 301, again can import the hot water of discharging in heat exchanger plate 1 in cooling tower 3 or frozen water machine 2 and lower the temperature.Heat exchanger plate 1, be provided with multiple valve between frozen water machine 2 and cooling tower 3, to control switch and the Flow-rate adjustment of hot water or cold water in pipeline.
When external environment is lower, cooling tower 3 can be only used to lower the temperature during use, close the switch before and after frozen water machine 2, open other switches, when external environment is higher (annual 6,7, August), can cooling tower 3 and frozen water machine 2 with the use of, by adjust flux after all switch opens.Through estimation, use this HFCS production workshop section cooling system, the power consumption 43.86 ten thousand degree of annual total, the cooling system before comparing, 340,000 degree of electricity can be saved every year, make huge contribution for company is energy-conservation.
The above is preferred embodiment of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications are also considered as protection domain of the present utility model.
Claims (9)
1. a HFCS production workshop section cooling system, is characterized by: comprise the heat transmission equipment for carrying out cooling HFCS, in heat transmission equipment upstream and frozen water machine parallel with one another and cooling tower, intake pump between cooling tower and heat transmission equipment.
2. HFCS production workshop section according to claim 1 cooling system, is characterized by: described frozen water machine is provided with the first water inlet end and the first water side.
3. HFCS production workshop section according to claim 2 cooling system, it is characterized by: described cooling tower is arranged in unlimited tank, cooling tower upper end is provided with the second water inlet end and tank lower end is provided with the second water side, and cooling tower inner upper end is provided with fan.
4. HFCS production workshop section according to claim 3 cooling system, is characterized by: described frozen water machine is at least one, and described cooling tower is at least one.
5. HFCS production workshop section according to claim 1 cooling system, is characterized by: described heat transmission equipment is heat exchanger plate, and described heat exchanger plate is provided with cooling water inlet, hot water outlet, hot sugared import and cold sugar outlet.
6. the HFCS production workshop section cooling system according to Claims 2 or 3 or 5, is characterized by: described first water inlet end and the second water inlet end are respectively equipped with the first hot water pipeline and the second hot water pipeline; Described first water side and be respectively equipped with the first cold water pipes and the second cold water pipes between the second water side and the cooling water inlet of heat exchanger plate; The hot water outlet of described heat exchanger plate and be provided with the 3rd hot water pipeline between the first water inlet end and the second water inlet end.
7. HFCS production workshop section according to claim 1 cooling system, is characterized by: described heat transmission equipment, be provided with valve between frozen water machine and cooling tower.
8. HFCS production workshop section according to claim 1 cooling system, is characterized by: the refrigerating capacity of described frozen water machine is 125Kw, and energy consumption is for being 45Kw/h.
9. HFCS production workshop section according to claim 1 cooling system, is characterized by: the volume of described cooling tower is 500m
3, energy consumption is 18.5Kw/h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520921569.1U CN205138254U (en) | 2015-11-18 | 2015-11-18 | High fructose syrup production cooling system of workshop section |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520921569.1U CN205138254U (en) | 2015-11-18 | 2015-11-18 | High fructose syrup production cooling system of workshop section |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205138254U true CN205138254U (en) | 2016-04-06 |
Family
ID=55624040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520921569.1U Expired - Fee Related CN205138254U (en) | 2015-11-18 | 2015-11-18 | High fructose syrup production cooling system of workshop section |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205138254U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108363120A (en) * | 2018-04-19 | 2018-08-03 | 江苏瑞尔光学有限公司 | A kind of glasses lens plated machine Two-way Cycle ice water system |
-
2015
- 2015-11-18 CN CN201520921569.1U patent/CN205138254U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108363120A (en) * | 2018-04-19 | 2018-08-03 | 江苏瑞尔光学有限公司 | A kind of glasses lens plated machine Two-way Cycle ice water 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 |
Effective date of registration: 20200722 Address after: Group 16, xintuan neighborhood committee, Dongtai town, Dongtai City, Yancheng City, Jiangsu Province Patentee after: Dongtai Pinqing Biotechnology Co., Ltd Address before: 215300, No. 530 Qingyang North Road, Zhou Zhou Town, Suzhou, Jiangsu, Kunshan Patentee before: KUNSHAN PINQING BIOTECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160406 Termination date: 20191118 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |