CN104613455B - A kind of steam vulcanization (cure) rubber energy recovery integrated system - Google Patents
A kind of steam vulcanization (cure) rubber energy recovery integrated system Download PDFInfo
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- CN104613455B CN104613455B CN201510063432.1A CN201510063432A CN104613455B CN 104613455 B CN104613455 B CN 104613455B CN 201510063432 A CN201510063432 A CN 201510063432A CN 104613455 B CN104613455 B CN 104613455B
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Abstract
The invention discloses a kind of steam vulcanization (cure) rubber energy recovery integrated system, including 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 including is connected by a plurality of pipeline between softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator, vulcanizing tank and wastewater disposal basin, and the left end at softening equipment and steam boiler is circumscribed with pond and fuel cartridge from the beginning respectively.By arrangement above, the softening water in water tank of the present invention keeps constant temperature throughout the year, effectively reduces the consumption of fuel, and heat energy recycle rate is higher, effectively save Fuel Consumption.The present invention is provided with intelligence control system, can realize intelligentized control method, and be capable of two grades of heating, i.e. uses combustion tail gas and exhaust steam two grades heating, reduces the generation of high temperature exhaust steam, saves the energy.
Description
Technical field
The present invention relates to a kind of energy recovery integrated system, a kind of steam
Vulcanized rubber article energy recovery integrated system.
Background technology
Steam as a kind of cleaning, safety hot energy carrier in all trades and professions by extensively
General application.In industries such as chemical industry, weaving, food, steam vulcanization (cure) is as rubber system
The principal mode of product sulfuration, is widely used.
After rubber has vulcanized, the saturated vapor in vulcanizing tank is typically directly
It is emitted into air.Directly exhaust steam discharge is not only caused energy waste, water resource
Waste, more can increase the weight of greenhouse effect.
Summary of the invention
It is an object of the invention to provide that a kind of heat utilization rate is higher, discharge waste gas relatively
Less and the wasting of resources can be reduced, reach the steam vulcanization (cure) rubber system of energy-saving and emission-reduction purpose
Product energy recovery integrated system.
For achieving the above object, the present invention include softening equipment, high-performance heat exchanger,
Water tank, heat exchanger, steam boiler, air accumulator, vulcanizing tank and wastewater disposal basin, institute
State include softening equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler,
Connected by a plurality of pipeline between air accumulator, vulcanizing tank and wastewater disposal basin, set in softening
Standby and steam boiler left end is circumscribed with pond and fuel cartridge from the beginning respectively；
Described high-performance heat exchanger left end is connected with softening equipment by a pipeline, its
Upper end is provided with two pipelines, and the pipeline of left end is connected with water tank, and at this pipe
The lower end in road is provided with hot water water intaking valve, and the pipeline of right-hand member is connected with vulcanizing tank；
The left end of described water tank is provided with three pipelines, uppermost pipeline and steam
Boiler is connected, and middle and nethermost pipeline is connected with heat exchanger, bottom
Pipeline be connected with the pipeline from high-performance heat exchanger；
The left end of described heat exchanger is provided with a pipeline being connected with steam boiler,
A pipeline being connected with wastewater disposal basin it is provided with, at this pipeline in the bottom of heat exchanger
Left end be provided with heat exchanger discharge of wastewater valve, be provided with on the top of heat exchanger two with
The pipeline that water tank is connected；
The left end of described steam boiler is provided with three pipelines, the most successively with combustion
Gas tank, heat exchanger are connected with water tank, and the centre position of pipeline topmost
Being provided with gas emergency cut-off valve, its right-hand member is provided with one and is connected with air accumulator
Pipeline, be respectively arranged at two ends with steam boiler air outlet valve and sending in the left and right of this pipeline
Air valve；
The left end of described air accumulator is provided with a pipeline being connected with steam boiler,
It is respectively arranged at two ends with steam boiler air outlet valve and air delivery valve in the left and right of this pipeline, its
Right-hand member is provided with a pipeline being connected with vulcanizing tank, in the centre position of this pipeline
It is provided with vulcanizing tank intake valve；
Described vulcanizing tank left end is provided with a pipeline being connected with air accumulator, and should
The centre position of pipeline is provided with vulcanizing tank intake valve, is provided with two in the bottom of vulcanizing tank
The pipeline that bar is connected with wastewater disposal basin respectively at high-performance heat exchanger, at the pipeline in left side
Upper end be provided with vulcanizing tank air bleeding valve, the pipeline on right side be provided with vulcanizing tank waste water row
Putting valve, its bottom is connected with the pipeline from heat exchanger.
By arrangement above, the softening water in water tank of the present invention keeps permanent throughout the year
Temperature, effectively reduces the consumption of fuel, and heat energy recycle rate is higher, effectively
Save Fuel Consumption.The present invention is provided with intelligence control system, can realize intellectuality
Control, and be capable of two grades of heating, i.e. use combustion tail gas and exhaust steam two grades
Heating, reduces the generation of high temperature exhaust steam, saves the energy.
Accompanying drawing explanation
In conjunction with accompanying drawing, the present invention will be further described
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 kettle
Stove air outlet valve, 16, air delivery valve, 17, vulcanizing tank intake valve, 18, vulcanizing tank row
Air valve, 19, vulcanizing tank discharge of wastewater valve.
Detailed description of the invention
As it is shown in figure 1, the present invention include softening equipment 1, high-performance heat exchanger 2,
Water tank 3, heat exchanger 4, steam boiler 5, air accumulator 6, vulcanizing tank 7 and useless
Pond 8, described in include softening equipment 1, high-performance heat exchanger 2, water tank 3, heat exchange
Pass through between device 4, steam boiler 5, air accumulator 6, vulcanizing tank 7 and wastewater disposal basin 8
A plurality of pipeline 9 connects, outside the left end difference of softening equipment 1 and steam boiler 5
It is connected to pond 10 and fuel cartridge 11 from the beginning；
Described high-performance heat exchanger 2 left end is by a pipeline 9 with softening equipment 1 even
Connecing, its upper end is provided with two pipelines 9, and the pipeline 9 of left end is connected with water tank 3
Connect, and be provided with hot water water intaking valve 12 in the lower end of this pipeline 9, the pipeline 9 of right-hand member
It is connected with vulcanizing tank 7；
The left end of described water tank 3 is provided with three pipelines 9, uppermost pipeline 9
It is connected with steam boiler 5, middle and nethermost pipeline 9 and heat exchanger 4 phase
Connecting, 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 pipe being connected with steam boiler 5
Road 9, is provided with a pipeline being connected with wastewater disposal basin 8 in the bottom of heat exchanger 4
9, the left end at this pipeline 9 is provided with heat exchanger discharge of wastewater valve 13, at heat exchanger
The top of 4 is provided with two pipelines 9 being connected with water tank 3；
The left end of described steam boiler 5 is provided with three pipelines 9, the most successively
It is connected with fuel cartridge 11, heat exchanger 4 and water tank 3, and pipeline topmost
The centre position of 9 is provided with gas emergency cut-off valve 14, and its right-hand member is provided with one
The pipeline 9 being connected with air accumulator 6, sets respectively at the two ends, left and right of this pipeline 9
There are steam boiler air outlet valve 15 and air delivery valve 16；
The left end of described air accumulator 6 is provided with a pipe being connected with steam boiler 5
Road 9, is respectively arranged at two ends with steam boiler air outlet valve 15 He in the left and right of this pipeline 9
Air delivery valve 16, its right-hand member is provided with a pipeline 9 being connected with vulcanizing tank 7,
The centre position of this pipeline 9 is provided with vulcanizing tank intake valve 17；
Described vulcanizing tank 7 left end is provided with a pipeline being connected with air accumulator 9,
And the centre position of this pipeline 9 is provided with vulcanizing tank intake valve 17, at vulcanizing tank 7
Bottom is provided with two pipelines being connected respectively at high-performance heat exchanger 2 with wastewater disposal basin 8
9, it is provided with vulcanizing tank air bleeding valve 18 in the upper end of the pipeline 9 in left side, the pipe on right side
Road 9 is provided with vulcanizing tank discharge of wastewater valve 19, its bottom with from heat exchanger 4
Pipeline 9 is connected.
By arrangement above, the operation principle of the present invention is as follows:
One-level heats: tap water, after softening equipment 1 softens, enters efficiently
Heat exchanger 2, waits to be heated；After product has vulcanized, the vulcanizing tank of vulcanizing tank 7
Air bleeding valve 18 is opened, and the waste gas that vulcanizing tank 7 is discharged enters in high-performance heat exchanger 2
Row thermal energy exchange, makes water temperature rise to more than 40 DEG C, enters water tank 3 stand-by,
When water tank 3 liquid level arrives peak, temporarily the softening water of heating is stored in
In high-performance heat exchanger 2.
Two grades of heating: steam boiler 5 is in opening, by using steam kettle
Stove 5 carries out the manufacture of steam and uses；The waste gas produced after steam boiler 5 burning
By heat exchanger 4, heat exchanger 4 uses steam boiler burning waste gas heating, will change
Softening water in hot device 4 is heated to 60 DEG C to 90 DEG C, it is achieved two grades of heating.
Steam boiler 5 uses liquefied gas burning to enter the softening water of 60 DEG C to 90 DEG C
Row heating manufactures the steam producing more than 1MPa, 2ton/h, and the steam of production enters
Being transported to the gas-distributing cylinder before vulcanizing tank 7 after entering air accumulator 6 voltage stabilizing, steam arrives and divides
The temperature of cylinder is more than 170 DEG C, and steam is in sub-cylinder is transported to vulcanizing tank 7
Carry out sulfuration to use；Steam after use participates in energy recovery.
Steam manufacture uses flow process: entered softening tap water by secondary heating system
After row heating, steam boiler is used to carry out making and the use of 170 DEG C of saturated vapors；
Softening water in water tank 3 is delivered to steam boiler 5 and is carried out the manufacture of steam, manufactures
The steam completed is delivered to air accumulator 6 and is carried out steam voltage stabilizing, through undue after steam voltage stabilizing
Cylinder is transported in vulcanizing tank 7 use；Before steam enters vulcanizing tank 7, because of
For being provided with vulcanizing tank intake valve 17, when temperature is close to when setting lower limit temperature, vulcanize
Canister incoming gas valve 17 automatically opens up, and carries out supplementing steam, it is ensured that the life of rubber
Production. art condition.
Energy recovery uses flow process: the exhaust steam discharged after vulcanizing tank 7 sulfuration accesses efficiently
Heat exchanger 2, the softening water after being softened by softening equipment 1 is heated to 60 by 20 DEG C
More than DEG C, the water after heating delivers to water tank 3 by feed pump, then passes through boiler
5 waste gas discharged use high-performance heat exchanger 4 to carry out two grades of heating, and water temperature rises to 60
DEG C to 90 DEG C, steam boiler uses the softening water of 60 DEG C to 90 DEG C to carry out steam system
Make.
Claims (1)
1. a steam vulcanization (cure) rubber energy recovery integrated system, including soft
Change equipment, high-performance heat exchanger, water tank, heat exchanger, steam boiler, air accumulator,
Vulcanizing tank and wastewater disposal basin, it is characterised in that: described softening equipment, high-performance heat exchanger,
Between water tank, heat exchanger, steam boiler, air accumulator, vulcanizing tank and wastewater disposal basin
Connected by a plurality of pipeline, the most external at the left end of softening equipment and steam boiler
There are pond and fuel cartridge from the beginning；
Described high-performance heat exchanger left end is connected with softening equipment by a pipeline, its
Upper end is provided with two pipelines, and the pipeline of left end is connected with water tank, and at this pipe
The lower end in road is provided with hot water water intaking valve, and the pipeline of right-hand member is connected with vulcanizing tank；
The left end of described water tank is provided with three pipelines, uppermost pipeline and steam
Boiler is connected, and middle and nethermost pipeline is connected with heat exchanger, bottom
Pipeline be connected with the pipeline from high-performance heat exchanger；
The left end of described heat exchanger is provided with a pipeline being connected with steam boiler,
A pipeline being connected with wastewater disposal basin it is provided with, at this pipeline in the bottom of heat exchanger
Left end be provided with heat exchanger discharge of wastewater valve, be provided with on the top of heat exchanger two with
The pipeline that water tank is connected；
The left end of described steam boiler is provided with three pipelines, the most successively with combustion
Gas tank, heat exchanger are connected with water tank, and the centre position of pipeline topmost
Being provided with gas emergency cut-off valve, its right-hand member is provided with one and is connected with air accumulator
Pipeline, be respectively arranged at two ends with steam boiler air outlet valve and sending in the left and right of this pipeline
Air valve；
The left end of described air accumulator is provided with a pipeline being connected with steam boiler,
It is respectively arranged at two ends with steam boiler air outlet valve and air delivery valve in the left and right of this pipeline, its
Right-hand member is provided with a pipeline being connected with vulcanizing tank, in the centre position of this pipeline
It is provided with vulcanizing tank intake valve；
Described vulcanizing tank left end is provided with a pipeline being connected with air accumulator, and should
The centre position of pipeline is provided with vulcanizing tank intake valve, is provided with two in the bottom of vulcanizing tank
The pipeline that bar is connected with wastewater disposal basin respectively at high-performance heat exchanger, at the pipeline in left side
Upper end be provided with vulcanizing tank air bleeding valve, the pipeline on right side be provided with vulcanizing tank waste water row
Putting valve, its bottom is connected with the pipeline from heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510063432.1A CN104613455B (en) | 2015-02-09 | 2015-02-09 | A kind of steam vulcanization (cure) rubber energy recovery integrated system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| 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 CN104613455A (en) | 2015-05-13 |
| CN104613455B true CN104613455B (en) | 2016-08-24 |
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| 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 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5337426B2 (en) * | 2008-07-30 | 2013-11-06 | 株式会社三共 | Game machine |
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2015
- 2015-02-09 CN CN201510063432.1A patent/CN104613455B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
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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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