CN104815499A - Energy-saving self-preheating super refining apparatus and method thereof - Google Patents
Energy-saving self-preheating super refining apparatus and method thereof Download PDFInfo
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- CN104815499A CN104815499A CN201510167303.7A CN201510167303A CN104815499A CN 104815499 A CN104815499 A CN 104815499A CN 201510167303 A CN201510167303 A CN 201510167303A CN 104815499 A CN104815499 A CN 104815499A
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Abstract
The invention relates to the petroleum refining field, and concretely relates to an energy-saving self-preheating super refining apparatus and a method thereof. The apparatus comprises a compressed air inlet pipeline, compression gauges, filters, a super refining apparatus body and a compressed air outlet pipeline; the compressed air inlet pipeline, the super refining apparatus body and the compressed air outlet pipeline are connected in order, the compression gauges and filters are provided, and the energy-saving self-preheating super refining apparatus comprises a temperature measurement mechanism and an exhaust mechanism. The temperature measurement mechanism comprises a top temperature sensor, a bottom temperature sensor and a temperature controller, the exhaust mechanism also comprises an evacuation valve, an evacuation valve solenoid valve and a compressed air pipeline solenoid valve. The temperature of the super refining apparatus body can be measured by the temperature measurement mechanism, opening and closing of the solenoid valve in the exhaust mechanism can be automatically controlled without artificial intervention, labor force is saved, work efficiency is increased, and energy waste is reduced. A muffler is equipped on the solenoid valve of an evacuation valve, and noise pollution is effectively reduced.
Description
Technical field
The present invention relates to oil refining field, especially relate to a kind of can save energy from the super refinery device and method of preheating.
Background technology
Super refinery device is a kind of compressed-air actuated a kind of device be converted into by the compressed air containing micro-oil without oil, only have and the oil in compressed air could be transformed non-oil gas when this device internal temperature reaches certain value, and when device internal temperature does not reach standard, the micro-oily compressed air through super refinery device still contains oil.
Traditional settling mode is at bottom of device and top mounting heater respectively, when super refinery plant running, and these 2 heater work.But refinery device initial start stage, temperature does not reach 220 DEG C, and refinery compressed air does not in earlier stage reach technological requirement, can not be transported to workshop.Whether traditional mode can not automatic gauging temperature, micro-judgment air can only be leaned on up to standard, cannot transmit in time, cause the waste of the energy to air up to standard.
Summary of the invention
Object of the present invention be exactly a kind of labour of saving be provided in order to overcome defect that above-mentioned prior art exists, increase work efficiency, energy-efficient, can the super refinery device and method of automatic preheating.
Object of the present invention can be achieved through the following technical solutions:
A kind of can save energy from the super refinery device of preheating, comprise compressed air inlet pipe road, Pressure gauge, filter, super refinery device body and compressed air outlet pipe, described compressed air inlet pipe road, super refinery device body is connected successively with compressed air outlet pipe, described Pressure gauge and filter have multiple, be arranged on the pipeline of device, described super refinery device body is provided with top heater and bottom heater, it is characterized in that, also comprise temperature measuring mechanism and exhaust gear, described temperature measuring mechanism one end is connected with super refinery device body, the other end is connected with exhaust gear, control the action of exhaust gear, described exhaust gear is connected with compressed air outlet pipe, control the flowing of air in compressed air outlet pipe.
Described temperature measuring mechanism comprises head temperature sensor, bottom temp sensor and temperature controller, described head temperature sensor and bottom temp sensor are arranged on top heater and bottom heater respectively, head temperature sensor is connected the input of temperature controller respectively with the output of bottom temp sensor, and the output of temperature controller connects exhaust gear.
Described exhaust gear comprises exhaust-valve, exhaust-valve magnetic valve and compressed air piping magnetic valve, described exhaust-valve one end connects compressed air outlet pipe, the other end connects exhaust-valve magnetic valve, described compressed air piping magnetic valve is arranged on compressed air outlet pipe, and exhaust-valve magnetic valve is connected the output of temperature controller respectively with the valve body of compressed air piping magnetic valve.
Described exhaust gear also comprises muffler, and described muffler is connected with exhaust-valve magnetic valve.
The pre-heating mean from the super refinery device of preheating that can save energy, comprises the following steps:
(1) anhydrous micro-oily air enters super refinery device body by compressed air inlet pipe, and now emptying solenoid valve and exhaust-valve are in opening, and compressed air piping magnetic valve is in closed condition, and compressed air is discharged by exhaust-valve;
(2) top heater and bottom heater start;
(3) temperature of head temperature sensor test top heater, and temperature signal is converted to electric signal transmission to temperature controller, if temperature reaches setting value, then enter step (4); If not, then step (3) is returned;
(4) temperature of bottom temp sensor test bottom heater, and temperature signal is converted to electric signal transmission to temperature controller, if temperature reaches setting value, then enter step (5); If not, then step (4) is returned;
(5) temperature controller control exhaust-valve magnetic valve makes it cut out, simultaneous temperature controller controls compressed air piping magnetic valve makes it open, compressed air is transported to workshop station by compressed air outlet pipe, refinery state is entered, now manual-lock exhaust-valve from the super refinery device of preheating.
Compared with prior art, the present invention has the following advantages:
(1) by temperature sensor automatic detection device internal temperature, do not need manual intervention, save labour, increase work efficiency.
(2) temperature controller controls the magnetic valve on compressed air outlet pipe automatically, once temperature controller detects up to standard, then brings into use compressed air up to standard, avoids the energy waste that traditional approach causes.
(3) exhaust-valve magnetic valve is equipped with muffler, effectively reduces air and discharge the noise pollution produced.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention, and in figure, 1 is compressed air inlet pipe road, 2 is Pressure gauge, and 3 is filter, and 4 is super refinery device body, 5 is head temperature sensor, 6 is bottom temp sensor, and 7 is temperature controller, and 8 is exhaust-valve, 9 is exhaust-valve magnetic valve, 10 is muffler, and 11 is compressed air piping magnetic valve, and 12 is compressed air outlet pipe;
Fig. 2 is the pre-heating mean flow chart of this device.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention is described in detail.The present embodiment is implemented premised on technical solution of the present invention, give detailed embodiment and concrete operating process, but protection scope of the present invention is not limited to following embodiment.
Embodiment 1
As shown in Figure 1, this device comprises compressed air inlet pipe road 1, Pressure gauge 2, filter 3, super refinery device body 4, head temperature sensor 5, bottom temp sensor 6, temperature controller 7, exhaust-valve 8, exhaust-valve magnetic valve 9, muffler 10, compressed air piping magnetic valve 11 and compressed air outlet pipe 12.
Compressed air inlet pipe road 1, super refinery device body 4 are connected successively with compressed air outlet pipe 12.
Pressure gauge 2 has two, and filter 3 has three, and first Pressure gauge 2 and the first two filter 3 are arranged on compressed air inlet pipe road 1, and second Pressure gauge 2 and the 3rd filter 3 are arranged on as on compressed air outlet pipe 12.
Head temperature sensor 5, bottom temp sensor 6 and temperature controller 7 form temperature measuring mechanism, wherein, head temperature sensor 5 and bottom temp sensor 6 are arranged on top heater and bottom heater respectively, and head temperature sensor 5 is connected the input of temperature controller 7 respectively with the output of bottom temp sensor 6.
Exhaust-valve 8, exhaust-valve magnetic valve 9, compressed air piping magnetic valve 11 and muffler 10 form exhaust gear.Exhaust-valve 8 one end connects compressed air outlet pipe 12, the other end connects exhaust-valve magnetic valve 9, compressed air piping magnetic valve 11 is arranged on compressed air outlet pipe 12, and exhaust-valve magnetic valve 9 is all connected the output of temperature controller 7 with the valve body of compressed air piping magnetic valve 11.Muffler 10 is connected with exhaust-valve magnetic valve 9.
As shown in Figure 2, the pre-heating mean of this device comprises the following steps:
S01, is positioned at the valve open on compressed air inlet pipe 1, and anhydrous micro-oily air is entered endlessly by compressed air inlet pipe 1, and through Pressure gauge 2 pressure measurement, preferably, air pressure is 13bar.Then filter through two filters 3, enter super refinery device body 4, carry out initial stage refinery.Now emptying solenoid valve 9 and exhaust-valve 8 are in opening, and compressed air piping magnetic valve 11 is in closed condition, and compressed air is discharged by exhaust-valve 8.
S02, top heater and bottom heater start, and carry out preheating to super refinery device body 4.
S03, the temperature of top heater tested by head temperature sensor 5, and temperature signal is converted to electric signal transmission to temperature controller 7, if temperature reaches setting value, then enters step S04; If not, then step S03 is returned.Preferably, preset temperature is 220 DEG C.
S04, when top heater temperature is just up to standard, bottom temp is also below standard.The temperature of now bottom temp sensing 6 device test bottom heater, and temperature signal is converted to electric signal transmission to temperature controller 7, if temperature reaches setting value, then enter step S05; If not, then step S04 is returned.
S05, temperature controller 7 controls exhaust-valve magnetic valve 9 makes it close, simultaneous temperature controller 7 controls compressed air piping magnetic valve 11 makes it open, and compressed air, through second Pressure gauge 3 and the 3rd filter 2, is transported to workshop station by compressed air outlet pipe 12.
Now preheating terminates, and enters refinery state from the super refinery device of preheating, and anhydrous micro-oily air constantly enters compressed air inlet pipe 1, and top heater and bottom heater keep heated condition.Relevant staff can manual-lock exhaust-valve 8, prevents air leak.
Claims (5)
1. one kind can save energy from the super refinery device of preheating, comprise compressed air inlet pipe road, Pressure gauge, filter, super refinery device body and compressed air outlet pipe, described compressed air inlet pipe road, super refinery device body is connected successively with compressed air outlet pipe, described Pressure gauge and filter have multiple, be arranged on the pipeline of device, described super refinery device body is provided with top heater and bottom heater, it is characterized in that, also comprise temperature measuring mechanism and exhaust gear, described temperature measuring mechanism one end is connected with super refinery device body, the other end is connected with exhaust gear, control the action of exhaust gear, described exhaust gear is connected with compressed air outlet pipe, control the flowing of air in compressed air outlet pipe.
2. according to claim 1 can save energy from the super refinery device of preheating, it is characterized in that, described temperature measuring mechanism comprises head temperature sensor, bottom temp sensor and temperature controller, described head temperature sensor and bottom temp sensor are arranged on top heater and bottom heater respectively, head temperature sensor is connected the input of temperature controller respectively with the output of bottom temp sensor, and the output of temperature controller connects exhaust gear.
3. according to claim 2 can save energy from the super refinery device of preheating, it is characterized in that, described exhaust gear comprises exhaust-valve, exhaust-valve magnetic valve and compressed air piping magnetic valve, described exhaust-valve one end connects compressed air outlet pipe, the other end connects exhaust-valve magnetic valve, described compressed air piping magnetic valve is arranged on compressed air outlet pipe, and exhaust-valve magnetic valve is connected the output of temperature controller respectively with the valve body of compressed air piping magnetic valve.
4. according to claim 3 can save energy from the super refinery device of preheating, it is characterized in that, described exhaust gear also comprises muffler, and described muffler is connected with exhaust-valve magnetic valve.
5. the pre-heating mean from the super refinery device of preheating that can save energy as claimed in claim 3, is characterized in that, comprise the following steps:
(1) anhydrous micro-oily air enters super refinery device body by compressed air inlet pipe, and now emptying solenoid valve and exhaust-valve are in opening, and compressed air piping magnetic valve is in closed condition, and compressed air is discharged by exhaust-valve;
(2) top heater and bottom heater start;
(3) temperature of head temperature sensor test top heater, and temperature signal is converted to electric signal transmission to temperature controller, if temperature reaches setting value, then enter step (4); If not, then step (3) is returned;
(4) temperature of bottom temp sensor test bottom heater, and temperature signal is converted to electric signal transmission to temperature controller, if temperature reaches setting value, then enter step (5); If not, then step (4) is returned;
(5) temperature controller control exhaust-valve magnetic valve makes it cut out, simultaneous temperature controller controls compressed air piping magnetic valve makes it open, compressed air is transported to workshop station by compressed air outlet pipe, refinery state is entered, now manual-lock exhaust-valve from the super refinery device of preheating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167303.7A CN104815499B (en) | 2015-04-09 | 2015-04-09 | A kind of super refinery device and method of preheating certainly that can save energy |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510167303.7A CN104815499B (en) | 2015-04-09 | 2015-04-09 | A kind of super refinery device and method of preheating certainly that can save energy |
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| CN104815499A true CN104815499A (en) | 2015-08-05 |
| CN104815499B CN104815499B (en) | 2016-08-24 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005344543A (en) * | 2004-06-01 | 2005-12-15 | Eiichi Uratani | Device and method for supplying compressed air |
| CN202376897U (en) * | 2011-12-29 | 2012-08-15 | 威海柳道机械有限公司 | Dehumidification type compressed air drying machine |
| US8574342B1 (en) * | 2010-12-27 | 2013-11-05 | Charles M. Flowe | Method and apparatus for membrane separation |
| CN203899424U (en) * | 2014-06-20 | 2014-10-29 | 中国电子工程设计院 | Energy-saving treatment system for high-flow compressed air |
| CN204637863U (en) * | 2015-04-09 | 2015-09-16 | 仪征祥源动力供应有限公司 | A kind of can save energy from the super refinery device of preheating |
-
2015
- 2015-04-09 CN CN201510167303.7A patent/CN104815499B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005344543A (en) * | 2004-06-01 | 2005-12-15 | Eiichi Uratani | Device and method for supplying compressed air |
| US8574342B1 (en) * | 2010-12-27 | 2013-11-05 | Charles M. Flowe | Method and apparatus for membrane separation |
| CN202376897U (en) * | 2011-12-29 | 2012-08-15 | 威海柳道机械有限公司 | Dehumidification type compressed air drying machine |
| CN203899424U (en) * | 2014-06-20 | 2014-10-29 | 中国电子工程设计院 | Energy-saving treatment system for high-flow compressed air |
| CN204637863U (en) * | 2015-04-09 | 2015-09-16 | 仪征祥源动力供应有限公司 | A kind of can save energy from the super refinery device of preheating |
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| CN104815499B (en) | 2016-08-24 |
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