CN204787914U - A constant temperature equipment for vapour congeals water -cooled - Google Patents
A constant temperature equipment for vapour congeals water -cooled Download PDFInfo
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- CN204787914U CN204787914U CN201520455359.8U CN201520455359U CN204787914U CN 204787914 U CN204787914 U CN 204787914U CN 201520455359 U CN201520455359 U CN 201520455359U CN 204787914 U CN204787914 U CN 204787914U
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- water
- cooling tower
- vapour
- described cooling
- cooled
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Abstract
The utility model discloses a constant temperature equipment for vapour congeals water -cooled, including cooling tower, water pump, fan and with the controller that is connected is held to the control input of water pump and fan, it has water inlet and air intake to open on the cooling tower, the input of water pump external to high temperature vapour water congeals, the output passes through the pipe connection and arrives on the water inlet of cooling tower, form high temperature vapour and congeal the adjustable input circuit of discharge, the external atmosphere of input of fan, output pass through the pipe connection and arrive on the air intake of cooling tower, form the adjustable input circuit of air current flow, the flow of controller control fan's the air current and the high temperature comdenstion water of water pump is according to a constant flow proportion through the air current to the cooling of dispelling the heat of high temperature comdenstion water. The utility model discloses make in the sugaring produced vapour congeal hydroenergy all by cyclic utilization once more, saved greatly and boiled the required energy in the sugared technology, have automatic temperature regulation, energy -concerving and environment -protective and reliable and stable beneficial effect.
Description
Technical field
The utility model belongs to sugar mill technical field, relates to a kind of thermostat, refers in particular to a kind of thermostat coagulating water-cooled for vapour.
Background technology
In sugar manufacturing industry, the sugar boiling technology step in sugaring process is required that the temperature of hot water used is within the specific limits constant, as 65 ~ 70 DEG C.The hot water of steady temperature is conducive to massecuite in crystallizing tank and avoids causing because being subject to the too low or too high impact of temperature massecuite because of the serious quality problems producing antiquated sand or molten sugar that are upset.
At present, the hot water that Sugar House adopts, general is all adopt hot water and the continuous mixing preparation of cold water to carry out temperature regulable control, and this kind of temperature regulates exists following shortcoming: in change low when 1, the water temperature of hot water is in height when occurring, stablizing of considerable influence cane sugar boiling and crystal; 2, the hot water used is that non-vapour coagulates water, and the quantity making the high-quality high temperature vapour produced in refining sugar coagulate water cannot be fully used, and makes utilize insufficient thus cause energy waste and environmental pollution.
Therefore, design one utilizes high temperature vapour to coagulate water as boiling sugar hot water completely, can save energy consumption, be conducive to the energy resource structure improving sugar enterprise, promotes that sugar enterprise is to energy-conservation and future development that is environment.
Utility model content
The purpose of this utility model be solve existing boil sugared hot water exist temperature stability difference and the high-quality high temperature vapour produced in sugaring cannot be used completely to coagulate water, and cause the problem of energy waste and environmental pollution, provide a kind of temperature control to regulate, stablize and the thermostat coagulating water-cooled for vapour of energy-conserving and environment-protective.
The purpose of this utility model can reach by the following technical solutions:
A kind of thermostat coagulating water-cooled for vapour, the controller comprising cooling tower, water pump, blower fan and be connected with the control input end of blower fan with described water pump, described cooling tower has water inlet and air inlet, the input of described water pump is external to high temperature vapour and coagulates water, output and be connected to by pipeline on the water inlet of described cooling tower, forms high temperature vapour and coagulates the adjustable input circuit of discharge; The external air of input, the output of described blower fan are connected to by pipeline on the air inlet of described cooling tower, form the adjustable input circuit of air flow rate; Described controller controls the flow of the air-flow of blower fan and the high-temperature condensation water of water pump, carries out radiating and cooling in certain flow ratio by air-flow to high-temperature condensation water.
As the preferred scheme of one, be provided with distributor in described cooling tower, the input of described distributor is connected to the water inlet of described cooling tower by pipeline.
As the improvement to cooling tower, described cooling tower is provided with at least one deck taper guide plate, and the diameter of described taper guide plate reduces from top to bottom gradually.
As the preferred scheme of one, the water inlet of described cooling tower is located at the top of the air inlet of described cooling tower.
As the further improvement to cooling tower, the upper/lower terminal of described cooling tower has gas outlet and delivery port, and described gas outlet is communicated with air.
As the improvement to controller, the delivery port of described cooling tower is provided with temperature sensor, and the output of described temperature sensor is connected with the detection input of described controller.
As the preferred scheme of one, be serially connected with flowmeter between the water inlet of described cooling tower and water pump and between the air inlet of described cooling tower and blower fan, the output of described flowmeter is connected with the detection input of described controller.
As the preferred scheme of one, below the delivery port of described cooling tower, be provided with the casing be connected with the delivery port of described cooling tower.
Implement the utility model, there is following beneficial effect:
1, the utility model adopts air-cooled form to coagulate water to high temperature vapour and cools, automatically allotment control is carried out to the discharge matching ratio of blower fan and water pump by controller, make to flow into the high temperature vapour of cooling tower and coagulate water by air-cooled and cool to the temperature value of setting and keep constant, with suitable hot water temperature's requirement of boiling needed for sugar, thus the vapour that produces coagulates water and all can be re-circulated utilization in making to refine sugar, and make the vapour sugar coagulated in water can separate out and improve the quantum of output of sugar, greatly save the energy required in sugar boiling technology, there is automation temperature regulate, energy-conserving and environment-protective and reliable and stable feature.
2, the water quality that the vapour that the utility model adopts coagulates water is outstanding, impurity content is few, can greatly improve the White Sugar Quality of making, solve and boil many by water impurity appetite with in the temperature-controlled process of hot water temperature of sugar in hot water and cold water mix to regulate, easily cause impurity to enter white granulated sugar thus cause the problem that the White Sugar Quality of making declines.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the utility model coagulates the thermostatically-controlled equipment of water-cooled structural representation for vapour.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Embodiment
See Fig. 1, the controller 4 that the present embodiment comprises cooling tower 1, water pump 2, blower fan 3 and is connected with the control input end of blower fan 3 with described water pump 2, described cooling tower 1 has water inlet and air inlet, the input of described water pump 2 is external to high temperature vapour and coagulates water, output and be connected to by pipeline on the water inlet of described cooling tower 1, forms high temperature vapour and coagulates the adjustable input circuit of discharge; The external air of input, the output of described blower fan 3 are connected to by pipeline on the air inlet of described cooling tower 1, form the adjustable input circuit of air flow rate; Described controller 4 controls the flow of the air-flow of blower fan 3 and the high-temperature condensation water of water pump 2, carries out radiating and cooling in certain flow ratio by air-flow to high-temperature condensation water.This device adopts air-cooled form to coagulate water to high temperature vapour and cools, automatically allotment control is carried out to the discharge matching ratio of blower fan 3 and water pump 2 by controller 4, make to flow into the high temperature vapour of cooling tower 1 and coagulate water by air-cooled and cool to the temperature value of setting and keep constant, with suitable hot water temperature's requirement of boiling needed for sugar, thus the vapour that produces coagulates water and all can be re-circulated utilization in making to refine sugar, and make the vapour sugar coagulated in water can separate out and improve the quantum of output of sugar, greatly save the energy required in sugar boiling technology, environmental protection, be conducive to the raising of Business Economic Benefit.
Better, be provided with distributor 5 in described cooling tower 1, the input of described distributor 5 is connected to the water inlet of described cooling tower 1 by pipeline.By distributor 5, high temperature vapour is coagulated water to send forth out, greatly can increase the cooling surface area that vapour coagulates water, vapour is coagulated object that water can realize fast cooling under the cooling of blower fan 3.
The water inlet of described cooling tower 1 is located at the top of the air inlet of described cooling tower 1.High temperature vapour coagulate water from cooling tower 1 water inlet through distributor 5 spray after, under gravity, to drop downwards motion, and in the process dropped, upwards blowing air-flow by blower fan 3 and coagulating water to high temperature vapour carries out air-cooled, the cool time making blower fan 3 pairs of high temperature vapour coagulate water is longer, is conducive to the effect increasing cooling.
Water time increase required the process of dropping is coagulated in order to make the high temperature vapour ejected from distributor 5, to promote the cooling effect of blower fan 3 further, described cooling tower 1 is provided with at least one deck taper guide plate 11, the diameter of described taper guide plate 11 reduces from top to bottom gradually, part vapour coagulates water under the obstruction of taper guide plate 11, lower ending opening through taper guide plate 11 continues to move downward, thus substantially increases the time of heat radiation.
The upper/lower terminal of described cooling tower 1 has gas outlet 12 and delivery port 13, and described gas outlet 12 is communicated with air.The casing 6 be connected with the delivery port 13 of described cooling tower 1 is provided with below the delivery port 13 of described cooling tower 1.Blower fan 3 pairs of high temperature vapour coagulate water to carry out air-cooled rear taken away heat and is upwards discharged to the outside in air through gas outlet 12, coagulated water by the vapour after lowering the temperature then to be discharged to downwards in casing 6 by delivery port 13 under gravity, thus realize vapour and coagulate the thermostatically controlled object of water-cooled.
The delivery port 13 of described cooling tower 1 is provided with temperature sensor 7, and the output of described temperature sensor 7 is connected with the detection input of described controller 4.Be serially connected with flowmeter 8 between the water inlet of described cooling tower 1 and water pump 2 and between the air inlet of described cooling tower 1 and blower fan 3, the output of described flowmeter 8 is connected with the detection input of described controller 4.Controller 4 is by the data of collecting temperature sensor 7, after the temperature value of the delivery port of the cooling tower 1 of data and setting is compared, according to the size of difference, adjustment outputs a control signal to water pump 2 and blower fan 3, make the flow proportional of water pump 2 and blower fan 3 increase or reduce, and pass through the detection data of acquisition stream gauge 8, in real time water pump 2 and blower fan 3 are carried out to the adjustment of flow error, to ensure the accurate in scale of water pump 2 and blower fan 3 flow further, thus realize the object that automatic constant-temperature controls.
Above disclosedly be only a kind of preferred embodiment of the utility model, certainly can not limit the interest field of the utility model with this, therefore according to the equivalent variations that the utility model claim is done, still belong to the scope that the utility model is contained.
Claims (8)
1. one kind is coagulated the thermostat of water-cooled for vapour, it is characterized in that: the controller comprising cooling tower, water pump, blower fan and be connected with the control input end of blower fan with described water pump, described cooling tower has water inlet and air inlet, the input of described water pump is external to high temperature vapour and coagulates water, output and be connected to by pipeline on the water inlet of described cooling tower, forms high temperature vapour and coagulates the adjustable input circuit of discharge; The external air of input, the output of described blower fan are connected to by pipeline on the air inlet of described cooling tower, form the adjustable input circuit of air flow rate; Described controller controls the flow of the air-flow of blower fan and the high-temperature condensation water of water pump, carries out radiating and cooling in certain flow ratio by air-flow to high-temperature condensation water.
2. a kind of thermostat coagulating water-cooled for vapour according to claim 1, is characterized in that: be provided with distributor in described cooling tower, and the input of described distributor is connected to the water inlet of described cooling tower by pipeline.
3. a kind of thermostat coagulating water-cooled for vapour according to claim 1 and 2, it is characterized in that: described cooling tower is provided with at least one deck taper guide plate, the diameter of described taper guide plate reduces from top to bottom gradually.
4. a kind of thermostat coagulating water-cooled for vapour according to claim 1 and 2, is characterized in that: the water inlet of described cooling tower is located at the top of the air inlet of described cooling tower.
5. a kind of thermostat coagulating water-cooled for vapour according to claim 1, is characterized in that: the upper/lower terminal of described cooling tower has gas outlet and delivery port, and described gas outlet is communicated with air.
6. a kind of thermostat coagulating water-cooled for vapour according to claim 5, is characterized in that: the delivery port of described cooling tower is provided with temperature sensor, and the output of described temperature sensor is connected with the detection input of described controller.
7. a kind of thermostat coagulating water-cooled for vapour according to claim 1, it is characterized in that: be serially connected with flowmeter between the water inlet of described cooling tower and water pump and between the air inlet of described cooling tower and blower fan, the output of described flowmeter is connected with the detection input of described controller.
8. a kind of thermostat coagulating water-cooled for vapour according to claim 5 or 6, is characterized in that: be provided with the casing be connected with the delivery port of described cooling tower below the delivery port of described cooling tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520455359.8U CN204787914U (en) | 2015-06-29 | 2015-06-29 | A constant temperature equipment for vapour congeals water -cooled |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520455359.8U CN204787914U (en) | 2015-06-29 | 2015-06-29 | A constant temperature equipment for vapour congeals water -cooled |
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| Publication Number | Publication Date |
|---|---|
| CN204787914U true CN204787914U (en) | 2015-11-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520455359.8U Expired - Fee Related CN204787914U (en) | 2015-06-29 | 2015-06-29 | A constant temperature equipment for vapour congeals water -cooled |
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| CN (1) | CN204787914U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104930875A (en) * | 2015-06-29 | 2015-09-23 | 广西农垦糖业集团红河制糖有限公司 | Thermostat used for condensate heat radiation |
| CN106017130A (en) * | 2016-06-27 | 2016-10-12 | 广西农垦糖业集团红河制糖有限公司 | Jet type hot water cooling device |
| JP2017166786A (en) * | 2016-03-18 | 2017-09-21 | 住友金属鉱山株式会社 | Counterflow direct heating type heat exchanger |
| WO2017159837A1 (en) * | 2016-03-18 | 2017-09-21 | 住友金属鉱山株式会社 | Countercurrent-type direct-heating heat exchanger |
-
2015
- 2015-06-29 CN CN201520455359.8U patent/CN204787914U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104930875A (en) * | 2015-06-29 | 2015-09-23 | 广西农垦糖业集团红河制糖有限公司 | Thermostat used for condensate heat radiation |
| JP2017166786A (en) * | 2016-03-18 | 2017-09-21 | 住友金属鉱山株式会社 | Counterflow direct heating type heat exchanger |
| WO2017159836A1 (en) * | 2016-03-18 | 2017-09-21 | 住友金属鉱山株式会社 | Countercurrent-type direct heating heat exchanger |
| WO2017159837A1 (en) * | 2016-03-18 | 2017-09-21 | 住友金属鉱山株式会社 | Countercurrent-type direct-heating heat exchanger |
| CN106017130A (en) * | 2016-06-27 | 2016-10-12 | 广西农垦糖业集团红河制糖有限公司 | Jet type hot water cooling device |
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| 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: 20151118 Termination date: 20190629 |
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| CF01 | Termination of patent right due to non-payment of annual fee |