CN104613455A - Steam vulcanized rubber product heat recovery comprehensive system - Google Patents
Steam vulcanized rubber product heat recovery comprehensive system Download PDFInfo
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- CN104613455A CN104613455A CN201510063432.1A CN201510063432A CN104613455A CN 104613455 A CN104613455 A CN 104613455A CN 201510063432 A CN201510063432 A CN 201510063432A CN 104613455 A CN104613455 A CN 104613455A
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Abstract
The invention discloses a steam vulcanized rubber product heat recovery comprehensive system which comprises a softening device, a high-efficiency heat exchanger, a water storage tank, a heat exchanger, a steam boiler, a gas storage tank, a vulcanizing tank and a waste water pool. The steam vulcanized rubber product heat recovery comprehensive system is characterized in that the softening device, the high-efficiency heat exchanger, the water storage tank, the heat exchanger, the steam boiler, the gas storage tank, the vulcanizing tank and the waste water pool are connected with one another through a plurality of pipelines, and the left end of the softening device and the left end of the steam boiler are externally connected with a tap water pool and the gas storage tank respectively. Through the arrangement, softened water in the water storage tank keeps the constant temperature all year round, the fuel consumption is effectively lowered, the heat recycling efficiency is high, and the consumed fuel is effectively saved. An intelligent control system is arranged, and therefore intelligent control can be achieved; secondary heating can be achieved, that is, secondary heating is achieved through combustion exhaust gas and waste steam; thus, high-temperature waste steam is reduced, and energy is saved.
Description
Technical field
The present invention relates to a kind of energy recovery integrated system, is a kind of steam vulcanization (cure) rubber energy recovery integrated system specifically.
Background technology
Steam is widely used in all trades and professions as a kind of clean, safe hot energy carrier.In industries such as chemical industry, weaving, food, steam vulcanization (cure), as the principal mode of rubber sulfuration, is widely used.
After rubber sulfuration completes, the saturated vapor in vulcanizing tank is generally directly disposed to air.Directly exhaust steam discharge is not only caused energy waste, water resource waste, more can increase the weight of greenhouse effects.
Summary of the invention
The object of this invention is to provide that a kind of heat utilization rate is higher, discharging waste gas is less and the wasting of resources can be reduced, reach the steam vulcanization (cure) rubber energy recovery integrated system of energy-saving and emission-reduction object.
For achieving the above object, the present invention includes softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator, vulcanizing tank and wastewater disposal basin, it is characterized in that: described in draw together softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator, connected by many pipelines between vulcanizing tank and wastewater disposal basin, be circumscribed with pond and fuel cartridge from the beginning respectively at the left end of softening equipment and steam boiler.
As preferably, described high-performance heat exchanger left end is connected with softening equipment by a pipeline, and its upper end is provided with two pipelines, and the pipeline of left end is connected with water tank, and is provided with hot water water intaking valve in the lower end of this pipeline, and the pipeline of right-hand member is connected with vulcanizing tank.
As preferably, the left end of described water tank is provided with three pipelines, and uppermost pipeline is connected with steam boiler, and middle and nethermost pipeline is connected with heat exchanger, and nethermost pipeline is connected with the pipeline from high-performance heat exchanger.
As preferably, the left end of described heat exchanger is provided with a pipeline be connected with steam boiler, be provided with a pipeline be connected with wastewater disposal basin in the bottom of heat exchanger, be provided with heat exchanger discharge of wastewater valve at the left end of this pipeline, be provided with two pipelines be connected with water tank on the top of heat exchanger.
As preferably, the left end of described steam boiler is provided with three pipelines, be connected with water tank with fuel cartridge, heat exchanger successively from top to bottom, and the centre position of pipeline is topmost provided with gas emergency cut-off valve, its right-hand member is provided with a pipeline be connected with air accumulator, is respectively equipped with steam boiler air outlet valve and air delivery valve at the two ends, left and right of this pipeline.
As preferably, the left end of described air accumulator is provided with a pipeline be connected with steam boiler, be respectively equipped with steam boiler air outlet valve and air delivery valve at the two ends, left and right of this pipeline, its right-hand member is provided with a pipeline be connected with vulcanizing tank, is provided with vulcanizing tank intake valve in the centre position of this pipeline.
As preferably, described vulcanizing tank left end is provided with a pipeline be connected with air accumulator, and the centre position of this pipeline is provided with vulcanizing tank intake valve, two pipelines be connected with wastewater disposal basin respectively at high-performance heat exchanger are provided with in the bottom of vulcanizing tank, vulcanizing tank air bleeding valve is provided with in the upper end of the pipeline in left side, the pipeline on right side is provided with vulcanizing tank discharge of wastewater valve, and its bottom is connected with the pipeline from heat exchanger.
By above setting, the demineralized water in water tank of the present invention keeps constant temperature throughout the year, effectively reduce the consumption of fuel, and heat energy recycle rate is higher, effectively saves Fuel Consumption.The present invention is provided with intelligence control system, can realize intelligentized control method, and can realize secondary heating, namely uses combustion tail gas and the heating of exhaust steam secondary, reduces the generation of high temperature exhaust steam, economize energy.
Accompanying drawing explanation
Now the present invention will be further described by reference to the accompanying drawings.
Fig. 1 is operation principle schematic diagram of the present invention.
In figure: 1, softening equipment, 2, high-performance heat exchanger, 3, water tank, 4, heat exchanger, 5, steam boiler, 6, air accumulator, 7, vulcanizing tank, 8, wastewater disposal basin, 9, pipeline, 10, from the beginning pond, 11, fuel cartridge, 12, hot water water intaking valve, 13, heat exchanger discharge of wastewater valve, 14, gas emergency cut-off valve, 15, steam boiler air outlet valve, 16, air delivery valve, 17, vulcanizing tank intake valve, 18, vulcanizing tank air bleeding valve, 19, vulcanizing tank discharge of wastewater valve.
Detailed description of the invention
As shown in Figure 1, the present invention includes softening equipment 1, high-performance heat exchanger 2, water tank 3, heat exchanger 4, steam boiler 5, air accumulator 6, vulcanizing tank 7 and wastewater disposal basin 8, describedly draw together softening equipment 1, high-performance heat exchanger 2, water tank 3, heat exchanger 4, steam boiler 5, air accumulator 6, connected by many pipelines 9 between vulcanizing tank 7 and wastewater disposal basin 8, be circumscribed with pond 10 and fuel cartridge 11 from the beginning respectively at the left end of softening equipment 1 and steam boiler 5.
Described high-performance heat exchanger 2 left end is connected with softening equipment 1 by a pipeline 9, and its upper end is provided with two pipelines 9, and the pipeline 9 of left end is connected with water tank 3, and is provided with hot water water intaking valve 12 in the lower end of this pipeline 9, and the pipeline 9 of right-hand member is connected with vulcanizing tank 7.
The left end of described water tank 3 is provided with three pipelines 9, and uppermost pipeline 9 is connected with steam boiler 5, and middle and nethermost pipeline 9 is connected with heat exchanger 4, and nethermost pipeline 9 is connected with the pipeline 9 from high-performance heat exchanger 2.
The left end of described heat exchanger 4 is provided with a pipeline 9 be connected with steam boiler 5, a pipeline 9 be connected with wastewater disposal basin 8 is provided with in the bottom of heat exchanger 4, be provided with heat exchanger discharge of wastewater valve 13 at the left end of this pipeline 9, be provided with two pipelines 9 be connected with water tank 3 on the top of heat exchanger 4.
The left end of described steam boiler 5 is provided with three pipelines 9, be connected with water tank 3 with fuel cartridge 11, heat exchanger 4 successively from top to bottom, and the centre position of pipeline 9 is topmost provided with gas emergency cut-off valve 14, its right-hand member is provided with a pipeline 9 be connected with air accumulator 6, is respectively equipped with steam boiler air outlet valve 15 and air delivery valve 16 at the two ends, left and right of this pipeline 9.
The left end of described air accumulator 6 is provided with a pipeline 9 be connected with steam boiler 5, steam boiler air outlet valve 15 and air delivery valve 16 is respectively equipped with at the two ends, left and right of this pipeline 9, its right-hand member is provided with a pipeline 9 be connected with vulcanizing tank 7, is provided with vulcanizing tank intake valve 17 in the centre position of this pipeline 9.
Described vulcanizing tank 7 left end is provided with a pipeline be connected with air accumulator 9, and the centre position of this pipeline 9 is provided with vulcanizing tank intake valve 17, two pipelines 9 be connected with wastewater disposal basin 8 respectively at high-performance heat exchanger 2 are provided with in the bottom of vulcanizing tank 7, vulcanizing tank air bleeding valve 18 is provided with in the upper end of the pipeline 9 in left side, the pipeline 9 on right side is provided with vulcanizing tank discharge of wastewater valve 19, and its bottom is connected with the pipeline 9 from heat exchanger 4.
By above setting, operation principle of the present invention is as follows:
One-level heats: running water, after softening equipment 2 is softening, enters high-performance heat exchanger 2, waits to be heated; After product sulfuration completes, the air bleeding valve 11 of vulcanizing tank 7 is opened, the waste gas that vulcanizing tank 7 is discharged carries out thermal energy exchange in high-performance heat exchanger 2, water temperature is made to rise to more than 40 DEG C, enter water tank 3 stand-by, when water tank 3 liquid level arrives peak, temporarily the demineralized water of heating is stored in high-performance heat exchanger 2.
Secondary heats: steam boiler 5 is in opening, carries out the manufacture of steam by using steam boiler 5 and uses; The waste gas produced after steam boiler 5 burns is by heat exchanger 4, and heat exchanger 4 uses steam boiler burnt gas to heat, and the demineralized water in heat exchanger 4 is heated 60 DEG C to 90 DEG C, realizes secondary heating.
Steam boiler 5 uses liquefied gas to burn to carry out heating to the demineralized water of 60 DEG C to 90 DEG C and manufactures production more than 1MPa, the steam of 2ton/h, the gas-distributing cylinder before vulcanizing tank 7 is transported to after the steam produced enters air accumulator 6 voltage stabilizing, the temperature that steam arrives gas-distributing cylinder is more than 170 DEG C, and steam is transported in vulcanizing tank 7 through sub-cylinder and carries out sulfuration use; Steam after use participates in energy recovery.
Steam manufacture uses flow process: after being heated softening running water by secondary heating system, uses steam boiler to carry out making and the use of 170 DEG C of saturated vapors; Demineralized water in water tank 3 delivers to the manufacture that steam boiler 5 carries out steam, and the steam manufactured is delivered to air accumulator 6 and carried out steam voltage stabilizing, is transported in vulcanizing tank 7 uses after steam voltage stabilizing through sub-cylinder; Before steam enters vulcanizing tank 7, because be provided with vulcanizing tank intake valve 17, when temperature is close to setting lower limit temperature, vulcanizing tank intake valve 17 is opened automatically, carries out supplementary steam, ensures the manufacturing condition of rubber.
Energy recovery uses flow process: the exhaust steam access high-performance heat exchanger 2 of discharging after vulcanizing tank 7 sulfuration, demineralized water after softening for softening equipment 1 is heated to more than 60 DEG C by 20 DEG C, water after heating delivers to water tank 3 by feed pump, the waste gas of being discharged by boiler 5 again uses high-performance heat exchanger 4 to carry out secondary heating, water temperature rises to 60 DEG C to more than 90 DEG C, and steam boiler uses the demineralized water of 60 DEG C to more than 90 DEG C to carry out steam manufacture.
Claims (7)
1. a steam vulcanization (cure) rubber energy recovery integrated system, comprise softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator, vulcanizing tank and wastewater disposal basin, it is characterized in that: described in comprise softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator, connected by many pipelines between vulcanizing tank and wastewater disposal basin, be circumscribed with pond and fuel cartridge from the beginning respectively at the left end of softening equipment and steam boiler.
2. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: described high-performance heat exchanger left end is connected with softening equipment by a pipeline, its upper end is provided with two pipelines, the pipeline of left end is connected with water tank, and being provided with hot water water intaking valve in the lower end of this pipeline, the pipeline of right-hand member is connected with vulcanizing tank.
3. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: the left end of described water tank is provided with three pipelines, uppermost pipeline is connected with steam boiler, middle and nethermost pipeline is connected with heat exchanger, and nethermost pipeline is connected with the pipeline from high-performance heat exchanger.
4. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: the left end of described heat exchanger is provided with a pipeline be connected with steam boiler, a pipeline be connected with wastewater disposal basin is provided with in the bottom of heat exchanger, be provided with heat exchanger discharge of wastewater valve at the left end of this pipeline, be provided with two pipelines be connected with water tank on the top of heat exchanger.
5. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: the left end of described steam boiler is provided with three pipelines, be connected with water tank with fuel cartridge, heat exchanger successively from top to bottom, and the centre position of pipeline is topmost provided with gas emergency cut-off valve, its right-hand member is provided with a pipeline be connected with air accumulator, is respectively equipped with steam boiler air outlet valve and air delivery valve at the two ends, left and right of this pipeline.
6. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: the left end of described air accumulator is provided with a pipeline be connected with steam boiler, steam boiler air outlet valve and air delivery valve is respectively equipped with at the two ends, left and right of this pipeline, its right-hand member is provided with a pipeline be connected with vulcanizing tank, is provided with vulcanizing tank intake valve in the centre position of this pipeline.
7. a kind of steam vulcanization (cure) rubber energy recovery integrated system according to claim 1, it is characterized in that: described vulcanizing tank left end is provided with a pipeline be connected with air accumulator, and the centre position of this pipeline is provided with vulcanizing tank intake valve, two pipelines be connected with wastewater disposal basin respectively at high-performance heat exchanger are provided with in the bottom of vulcanizing tank, vulcanizing tank air bleeding valve is provided with in the upper end of the pipeline in left side, the pipeline on right side is provided with vulcanizing tank discharge of wastewater valve, and its bottom is connected with the pipeline from heat exchanger.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510063432.1A CN104613455B (en) | 2015-02-09 | 2015-02-09 | A kind of steam vulcanization (cure) rubber energy recovery integrated system |
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| CN201510063432.1A CN104613455B (en) | 2015-02-09 | 2015-02-09 | A kind of steam vulcanization (cure) rubber energy recovery integrated system |
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| CN104613455A true CN104613455A (en) | 2015-05-13 |
| CN104613455B CN104613455B (en) | 2016-08-24 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108443849A (en) * | 2018-05-21 | 2018-08-24 | 浙江保尔力胶带有限公司 | A kind of recovery system and its processing method of steam multi-ladder thermal energy |
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| JP2010029563A (en) * | 2008-07-30 | 2010-02-12 | Sankyo Co Ltd | Game machine |
| CN102700036A (en) * | 2012-06-01 | 2012-10-03 | 苏州市宝苏矿冶设备有限公司 | Hot water vulcanization system |
| CN103723850A (en) * | 2012-03-30 | 2014-04-16 | 斯普瑞斯-萨克有限公司 | Steam plant and method of operating same |
| CN204062991U (en) * | 2014-08-29 | 2014-12-31 | 厦门银鹭食品集团有限公司 | Can industry retort exhausting heat energy recovery system |
| CN204513330U (en) * | 2015-02-09 | 2015-07-29 | 山东美晨先进高分子材料科技有限公司 | A kind of steam vulcanization (cure) rubber energy recovery integrated system |
-
2015
- 2015-02-09 CN CN201510063432.1A patent/CN104613455B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010029563A (en) * | 2008-07-30 | 2010-02-12 | Sankyo Co Ltd | Game machine |
| CN103723850A (en) * | 2012-03-30 | 2014-04-16 | 斯普瑞斯-萨克有限公司 | Steam plant and method of operating same |
| CN102700036A (en) * | 2012-06-01 | 2012-10-03 | 苏州市宝苏矿冶设备有限公司 | Hot water vulcanization system |
| CN204062991U (en) * | 2014-08-29 | 2014-12-31 | 厦门银鹭食品集团有限公司 | Can industry retort exhausting heat energy recovery system |
| CN204513330U (en) * | 2015-02-09 | 2015-07-29 | 山东美晨先进高分子材料科技有限公司 | A kind of steam vulcanization (cure) rubber energy recovery integrated system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108443849A (en) * | 2018-05-21 | 2018-08-24 | 浙江保尔力胶带有限公司 | A kind of recovery system and its processing method of steam multi-ladder thermal energy |
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Address after: 262200 600 North ten li four village, Weifang, Zhucheng, Weifang, Shandong Patentee after: Shandong Machen Industrial Group Co., Ltd. Address before: 262200 600 North ten li fort, Zhuzhou City, Weifang, Shandong Patentee before: SHANDONG MEICHEN ADVANCED POLYMER MATERIALS TECHNOLOGY CO., LTD. |
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