CN115554804A - Air conditioning system of pipeline production workshop - Google Patents
Air conditioning system of pipeline production workshop Download PDFInfo
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- CN115554804A CN115554804A CN202211191287.1A CN202211191287A CN115554804A CN 115554804 A CN115554804 A CN 115554804A CN 202211191287 A CN202211191287 A CN 202211191287A CN 115554804 A CN115554804 A CN 115554804A
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 40
- 238000004378 air conditioning Methods 0.000 title claims abstract description 18
- 238000010438 heat treatment Methods 0.000 claims abstract description 104
- 238000001179 sorption measurement Methods 0.000 claims abstract description 90
- 238000009833 condensation Methods 0.000 claims abstract description 63
- 230000005494 condensation Effects 0.000 claims abstract description 63
- 238000002485 combustion reaction Methods 0.000 claims abstract description 60
- 239000007789 gas Substances 0.000 claims abstract description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 58
- 239000002912 waste gas Substances 0.000 claims abstract description 52
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 238000001816 cooling Methods 0.000 claims abstract description 7
- 239000003507 refrigerant Substances 0.000 claims description 29
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 15
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 15
- 241001330002 Bambuseae Species 0.000 claims description 15
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 15
- 239000011425 bamboo Substances 0.000 claims description 15
- 238000009434 installation Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 13
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- 239000008187 granular material Substances 0.000 claims description 8
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 230000000087 stabilizing effect Effects 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 2
- 230000008676 import Effects 0.000 claims 1
- 239000010815 organic waste Substances 0.000 abstract description 23
- 239000000126 substance Substances 0.000 abstract description 13
- 238000010521 absorption reaction Methods 0.000 description 11
- 239000004033 plastic Substances 0.000 description 9
- 229920003023 plastic Polymers 0.000 description 9
- 231100000614 poison Toxicity 0.000 description 8
- 230000007096 poisonous effect Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention discloses an air conditioning system of a pipeline production workshop, wherein an air inlet device comprises a mixing box, a heat supply pipe, a normal temperature pipe and an air inlet pipe, wherein the heat supply pipe, the normal temperature pipe and the heat supply pipe are connected to the mixing box; in the waste gas combustion device, an air supply disc is used for conveying waste gas collected in a pipeline production workshop to a combustion cylinder, an igniter arranged in the combustion cylinder can ignite the organic waste gas, a spiral heating pipe is fixedly arranged in a heating kettle, and the combustion cylinder is communicated with a condensation dewatering device through a first communicating pipe; the condensation dewatering device is communicated with the heating kettle through a water supply pipe; the adsorption device is communicated with the cooling and dewatering device through a second communicating pipe. The invention can efficiently and conveniently purify the organic waste gas, so that the discharged waste gas meets the relevant discharge standard, and the utilization rate of chemical energy in the waste gas is improved.
Description
Technical Field
The invention relates to the technical field of waste gas treatment in pipeline production, in particular to an air conditioning system of a pipeline production workshop.
Background
The plastic pipe is a common product in production and life, such as a PP pipe and a PE pipe for water supply and heating. When production plastic conduit, need carry out hybrid heating to polymer organic matter raw and other materials and relevant batching to through relevant production facility with production department plastic conduit, because plastic conduit has organic waste gas output at the in-process of heating production, and then influences the air quality of pipeline workshop, when organic waste gas gathers in the pipeline workshop more, there is the explosion risk that takes place, consequently needs carry out effective processing to the organic waste gas that produces in the pipeline production process. To the equipment that is used for handling organic waste gas in the pipeline production process of tradition, there often exist waste gas treatment inefficiency, simple operation degree subalternation problem, be difficult to guarantee to wherein the effective absorption of poisonous and harmful substance. And the traditional waste gas treatment equipment also lacks application measures for chemical energy in the organic waste gas, thereby causing resource waste.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide an air conditioning system of a pipeline production workshop, which can efficiently and conveniently purify organic waste gas so as to enable the discharged waste gas to meet related discharge standards and improve the utilization rate of chemical energy in the waste gas.
The technical scheme adopted by the invention for realizing the purpose is as follows: the utility model provides an air conditioning system of pipeline workshop, includes air inlet unit, exhaust gas combustion device, condensation water trap, adsorption equipment, air inlet unit includes mixing box and is connected to heating pipe, normal atmospheric temperature pipe, the intake pipe on the mixing box, and normal atmospheric temperature pipe, heating pipe all communicate with external environment, and are connected with the spiral heating pipe of installing in exhaust gas combustion device on the heating pipe, and the intake pipe communicates to in the pipeline workshop to supply with steam in to the pipeline workshop.
The waste gas burner includes the combustion cylinder and arranges heating cauldron, the air feed dish in the combustion cylinder inner chamber, and heating cauldron, air feed dish are installed respectively in combustion cylinder top, bottom, and the air feed dish is arranged in carrying the waste gas of pipeline workshop collection to the combustion cylinder, and in the combustion cylinder still fixed mounting have arrange the some firearm in air feed dish top side, spiral heating pipe fixed mounting is in heating cauldron, the combustion cylinder is through first communicating pipe and condensation water trap intercommunication to with the remaining high temperature steam input condensation water installation through the burning in the combustion cylinder.
The condensation dewatering device is used for carrying out condensation treatment on residual high-temperature hot gas input into the condensation dewatering device and removing water vapor in the hot gas, and the condensation dewatering device is communicated with the heating kettle through a water supply pipe; the adsorption device is communicated with the cooling and dewatering device through a second communicating pipe, and the adsorption device stirs and adsorbs the gas input into the adsorption device.
In some of the implementations, in order to ensure that the air supply plate can uniformly convey the organic waste gas collected in the pipeline workshop to the combustion cylinder, and the organic waste gas is ignited by the igniter to be stably combusted in the combustion cylinder, the following technical scheme about the air supply plate and the matching parts on the air supply plate is provided.
The air supply plate is provided with an air supply pipeline, the upper surface of the air supply plate is uniformly provided with a waste gas nozzle communicated with the air supply pipeline, the air supply pipeline in the air supply plate is communicated with a pipeline workshop through a waste gas conveying pipe, and a first air supply pump is installed on the waste gas conveying pipe in a matched mode.
In some of them implementation, for guaranteeing that heating cauldron and heating supply pipe stable combination, guarantee simultaneously that the inside atmospheric pressure of heating cauldron is stable, can be to stabilizing the moisturizing in the heating cauldron, provide following technical scheme about heating cauldron and continuous components.
The heating pipe comprises two sections fixedly connected with the heating kettle, two ends of the spiral heating pipe are fixedly connected with the heating pipes at the two ends and are communicated with each other, a second air supply pump is installed on the heating pipe in a matched mode, the water supply pipe is communicated to the inner side of the top of the heating kettle, a first pressure pump is installed on the water supply pipe in a matched mode, and the top of the heating kettle is further communicated with a pressure stabilizing pipe and a water injection pipe.
For guaranteeing that the air feed dish can be in the inboard bottom stable installation of a combustion section of thick bamboo, guarantee that the heating kettle can be in the inboard top stable installation of a combustion section of thick bamboo, provide following technical scheme on the basis of a combustion section of thick bamboo.
The combustor is characterized in that a lower-layer mounting ring is fixedly connected to the inner wall of the combustion barrel, the air supply disc is fixedly mounted on the lower-layer mounting ring, an upper-layer mounting ring is fixedly connected to the outer wall of the top of the combustion barrel, and the heating kettle is fixedly mounted on the upper-layer mounting ring.
In some of the implementations, in order to ensure that the air inlet device can deliver hot air with a constant temperature to the heating workshop so as to heat the pipeline production workshop in an environment with low air temperature, the following technical scheme related to the air inlet device is provided.
All supporting the installing electromagnetic flow valve on normal atmospheric temperature pipe, the heating supply pipe, still supporting the installing third air feed pump on the normal atmospheric temperature pipe, heating supply pipe and mixing box intercommunication department fixed mounting have first temperature sensor, supporting the installing fourth air feed pump in the intake pipe, and intake pipe and mixing box intercommunication department fixed mounting have the second temperature sensor.
In some embodiments, in order to ensure that the condensation and water removal device can perform condensation and water removal on the high-temperature exhaust gas input into the condensation and water removal device, the following technical solutions are provided.
The condensation dewatering device comprises an outer sleeve and a condensation cylinder arranged at the top of the outer sleeve, the outer wall of the condensation cylinder is fixedly connected with a spiral channel wound in a spiral mode, the second communicating pipe is communicated with the top end of the inner side of the condensation cylinder, the first communicating pipe is communicated with the middle section of the outer sleeve, the water supply pipe is communicated with the bottom end of the inner side of the outer sleeve, the inner wall of the condensation cylinder is fixedly connected with a spiral condensation pipe, and refrigerant medium is filled in the spiral condensation pipe.
On the basis of the technical scheme of the condensation dewatering device, the following technical scheme is provided for ensuring that the cold medium in the spiral condensation pipe continuously maintains a low-temperature state so as to cool the high-temperature waste gas and collect water vapor in the high-temperature waste gas in a condensation way.
The spiral condenser is characterized in that a cooler is further arranged, a refrigerant inlet of the cooler is communicated with the bottom end of the spiral condenser pipe through a refrigerant inlet pipe, a refrigerant outlet of the cooler is communicated with the top end of the spiral condenser pipe through a refrigerant outlet pipe, and a second pressure pump is mounted on the refrigerant outlet pipe in a matched mode.
In some of them implementation, can handle the waste gas of inputing wherein for guaranteeing adsorption equipment to the effective absorption of poisonous and harmful substance, guarantee that exhaust gas accords with exhaust emission standard, provide following technical scheme about adsorption equipment.
Adsorption equipment includes an adsorption cylinder and the multilayer adsorption disc of fixed mounting in the adsorption cylinder, the second is intercommunication pipe and the inboard bottom intercommunication of an adsorption cylinder, and each layer adsorption disc is arranged in the second and is managed the top side of intercommunication department with the adsorption cylinder, and has seted up the absorption chamber in each layer adsorption disc, the upper and lower surface of adsorption disc all set up with the air vent that adsorbs the chamber intercommunication, it has granular activated carbon to add in the absorption chamber.
On above technical scheme basis about adsorption equipment, for guaranteeing that each layer adsorption disc can be stably installed in adsorbing a section of thick bamboo, guarantee simultaneously that the waste gas through adsorption treatment can be followed and adsorbed a section of thick bamboo and export, be provided with following technical scheme.
The inside wall of the adsorption cylinder is fixedly connected with a plurality of layers of mounting rings, the adsorption disc is fixedly mounted on the mounting rings, the bottom end of the adsorption cylinder is communicated with an exhaust pipe, and the exhaust pipe is arranged in an inverted U shape.
On above technical scheme basis about adsorption equipment, for avoiding leading to the granule active carbon to take place to bond because of carrying a small amount of steam by the waste gas of condensation water trap input, can effectively improve the adsorption efficiency of granule active carbon to poisonous and harmful substance simultaneously, provide following technical scheme.
The rotation installs the vertical installation axle of arranging in the adsorption cylinder, and installs the axle and keep rotating with each group adsorption disc and be connected, installs epaxial fixed mounting and has the stirring rake that the multilayer was evenly arranged, and each layer stirring rake arranges respectively in the absorption chamber in each layer adsorption disc, and the adsorption cylinder top is fixed mounting still has driving motor, and driving motor and installation axle power is connected.
The invention has the following beneficial effects: organic waste gas that produces to pipeline production workshop handles through waste gas burner, condensation water trap and adsorption equipment's order, can carry out high-efficient, convenient purification treatment with organic waste gas to make exhaust gas satisfy relevant emission standard, improve the utilization ratio of chemical energy in the waste gas, specifically embody as follows.
(1) The setting of helical coiled passage and spiral condenser pipe on the condensing cylinder can effectively improve the cooling to high temperature waste gas to the high temperature vapor that will carry wherein effectively condenses.
(2) Each layer adsorbs the setting of dish and stirring rake in adsorption equipment, can effectively avoid having the granular activated carbon of adsorption function to receive the vapor effect to take place to bond, can improve the adsorption effect to poisonous and harmful substance simultaneously.
(3) In the waste gas combustion device, can carry out effective utilization to the heat that the waste gas burning produced to satisfy the part or whole heat supply demand in pipeline production workshop, improve the energy utilization who discharges waste gas and use up the rate.
Drawings
FIG. 1 is a schematic view of the structure of the present invention;
FIG. 2 is a schematic view of the structure of FIG. 1 from another perspective;
FIG. 3 is a schematic view of the intake device and the exhaust gas combustion device after being cut;
FIG. 4 is a schematic view of a condensation dewatering device after being cut;
fig. 5 is a schematic structural view of the adsorption apparatus after being cut.
In the figure: 101 mixing box, 102 heating pipe, 103 normal temperature pipe, 104 air inlet pipe, 105 spiral heating pipe, 106 second air supply pump, 107 electromagnetic flow valve, 108 third air supply pump, 109 fourth air supply pump, 201 combustion cylinder, 202 heating kettle, 203 air supply disc, 204 igniter, 205 first communicating pipe, 206 waste gas nozzle, 207 waste gas conveying pipe, 208 first air supply pump, 209 lower layer mounting ring, 210 pressure maintaining pipe, 211 water injection pipe, 212 upper layer mounting ring, 301 water supply pipe, 302 second communicating pipe, 303 first pressure pump, 304 outer sleeve, 305 condenser, 306 spiral channel, 307 spiral condenser, 308 cooler, 309 refrigerant inlet pipe, 310 refrigerant outlet pipe, 311 second pressure pump, 401 adsorption cylinder, 402 adsorption disc, 403 adsorption cavity, 404 mounting ring, exhaust pipe 405, 406 mounting shaft, 407 stirring paddle, 408 driving motor.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-5, the technical solutions and related operating principles provided in the present application will be described with reference to the following embodiments.
Example 1
The utility model provides an air conditioning system of pipeline workshop, including air inlet unit, the exhaust gas combustion device, condensation water trap, adsorption equipment, air inlet unit includes mixing box 101 and is connected to heating pipe 102 on the mixing box 101, normal atmospheric temperature pipe 103, intake pipe 104, normal atmospheric temperature pipe 103, heating pipe 102 all communicates with external environment, and be connected with the spiral heating pipe 105 of installing in the exhaust gas combustion device on the heating pipe 102, intake pipe 104 communicates to in the pipeline workshop, with supply with steam in to the pipeline workshop.
The waste gas combustion device comprises a combustion cylinder 201 and a heating kettle 202 arranged in the inner cavity of the combustion cylinder 201, an air supply disc 203, the heating kettle 202, the air supply disc 203 is respectively installed at the top and the bottom of the combustion cylinder 201, the air supply disc 203 is used for conveying waste gas collected in a pipeline production workshop to the combustion cylinder 201, an igniter 204 arranged on the upper side of the air supply disc 203 is further fixedly installed in the combustion cylinder 201, a spiral heating pipe 105 is fixedly installed in the heating kettle 202, the combustion cylinder 201 is communicated with a condensation water removal device through a first communication pipe 205, and residual high-temperature hot gas after combustion in the combustion cylinder 201 is input into the condensation water removal device.
The condensation dewatering device carries out condensation treatment on the residual high-temperature hot gas input into the condensation dewatering device and removes water vapor in the hot gas, and the condensation dewatering device is communicated with the heating kettle 202 through a water supply pipe 301; the adsorption device is communicated with the cooling and dewatering device through a second communicating pipe 302, and the adsorption device stirs and adsorbs the gas input therein.
When production plastic conduit, need carry out hybrid heating to polyethylene material and relevant batching to through relevant production facility with production department plastic conduit, because plastic conduit has organic waste gas output at the in-process of heating production, and then influences the air quality in pipeline production workshop, when organic waste gas gathers in the pipeline workshop more, there is the explosion risk that takes place.
And the high temperature waste gas after the combustion processing in the combustion cylinder 201 carries high temperature vapor, and input to the condensation dewatering device and cool down the high temperature waste gas, and simultaneously collect the high temperature vapor condensation, and the liquid water of collection can be to supplying water in the heating kettle 202.
And conveying the waste gas treated by the condensation dewatering device to an adsorption device, and discharging toxic and harmful substances in the waste gas which is treated by the condensation dewatering device to the outside, thereby finishing the whole process of treating the organic waste gas.
Example 2
On the basis of example 1, an optimization and operating principle for an exhaust gas combustion device is provided.
In order to ensure that the gas supply plate 203 can uniformly convey the organic waste gas collected in the pipeline workshop to the combustion cylinder 201, and the igniter 204 ignites the organic waste gas in the combustion cylinder 201 for stable combustion, the following technical scheme about the gas supply plate 203 and the matching parts thereof is provided.
An air supply pipeline is arranged in the air supply disc 203, an exhaust gas nozzle 206 communicated with the air supply pipeline is uniformly arranged on the upper surface of the air supply disc 203, the air supply pipeline in the air supply disc 203 is communicated with a pipeline workshop through an exhaust gas conveying pipe 207, and a first air supply pump 208 is installed on the exhaust gas conveying pipe 207 in a matched mode.
When the first air supply pump 208 works, waste gas generated in the production process of each production device in a pipeline workshop can be conveyed to the air supply disc 203 along the waste gas conveying pipe 207, and due to the uniform arrangement of each group of waste gas spray nozzles 206 on the air supply disc 203, the organic waste gas sprayed into the combustion cylinder 201 can be ensured to be uniformly distributed, and then the organic waste gas is ignited by the igniter 204 and is combusted in the combustion cylinder 201. Clean water is added to the heating kettle 202 and heated by the organic waste gas being combusted, which in turn heats the spiral heating pipe 105 disposed in the heating kettle 202 to heat the outside air conveyed therein.
In order to ensure that the heating kettle 202 is stably combined with the heating pipe 102 and the internal pressure of the heating kettle 202 is stable, and water can be stably supplemented into the heating kettle 202, the following technical scheme about the heating kettle 202 and the connected components is provided.
The heating pipe 102 comprises two sections fixedly connected with the heating kettle 202, two ends of the spiral heating pipe 105 are fixedly connected with the heating pipe 102 at two ends and are communicated, a second air supply pump 106 is installed on the heating pipe 102 in a matched mode, the water supply pipe 301 is communicated to the inner side of the top of the heating kettle 202, a first pressure pump 303 is installed on the water supply pipe 301 in a matched mode, and the top of the heating kettle 202 is further communicated with a pressure stabilizing pipe 210 and a water injection pipe 211.
The outside air is sent from the heating pipe 102 to the spiral heating pipe 105 by the second air supply pump 106, and is heated by the heated clean water in the heating kettle 202, so that the temperature of the air in the spiral heating pipe 105 is raised and inputted into the mixing box 101.
The spiral heating pipe 105 has a structural feature that the staying time of the air in the heating kettle 202 can be prolonged, so that the air can be sufficiently heated.
And the waste gas that is through burning in the section of thick bamboo 201 is cooled down to among the condensation water trap, because contain alkane material in the organic waste gas, can generate a small amount of steam when fully burning, and need be to its water-cooling when pipeline production facility produces the plastic conduit, lead to carrying steam in the same of organic waste gas, and contain vapor in the waste gas after the burning heat treatment, can collect the vapor condensation after being handled by condensation water trap, the liquid water of collection keeps the higher temperature equally, and carry to heating kettle 202 in through first force (forcing) pump 303 and delivery pipe 301, with make-up water in the heating kettle 202. Meanwhile, clean water can be supplemented into the heating kettle 202 through the water injection pipe 211.
After the water in the heating kettle 202 is boiled, a large amount of water vapor exists to increase the internal air pressure, and the excessive water vapor can be discharged outside through the pressure stabilizing tube 210 to ensure that the internal air pressure of the heating kettle 202 tends to be stable.
For guaranteeing that air feed dish 203 can be at the inboard bottom stable installation of a burner 201, guarantee that heating kettle 202 can be at the inboard top stable installation of a burner 201, provide following technical scheme on a burner 201's basis.
The inner wall of the combustion cylinder 201 is fixedly connected with a lower-layer mounting ring 209, the air supply disc 203 is fixedly mounted on the lower-layer mounting ring 209, the outer wall of the top of the combustion cylinder 201 is fixedly connected with an upper-layer mounting ring 212, and the heating kettle 202 is fixedly mounted on the upper-layer mounting ring 212.
The upper mounting ring 212 and the lower mounting ring 209 are arranged to ensure that the heating kettle 202 and the air supply disc 203 are stably mounted in the combustion cylinder 201. Heating kettle 202 carries out fixed combination through fixing bolt and upper mounting ring 212, and air feed dish 203 likes to carry out fixed combination with lower floor's mounting ring 209 through fixed rou to the convenience carries out the dismouting maintenance to waste gas combustion device.
Example 3
In order to ensure that the air inlet device can convey hot air with constant temperature to the heating workshop so as to supply heat to the pipeline production workshop in an environment with low air temperature, the following technical scheme related to the air inlet device is provided.
The third air supply pump 108 can input the ambient room temperature air into the mixing box 101 along the room temperature pipe 103, the first temperature sensor can detect the temperature of the hot air conveyed in the heat supply pipe 102, and the second temperature sensor can detect the temperature of the hot air conveyed by the air inlet pipe 104 to the pipeline workshop. Through the degree of opening and shutting of controlling the electromagnetic flow valve 107 on heat supply pipe 102, the normal atmospheric temperature pipe 103, can control the flow of the air in the input mixing box 101 in the normal atmospheric temperature pipe 103, the heat supply pipe 102, through mixing box 101 to the air intensive mixing heat transfer of two kinds of different temperatures to by the fourth air feed pump 109 with the hot gas of specific temperature along the intake pipe 104 input in the pipeline workshop, in order to carry out the heat supply to the pipeline workshop.
In the high-temperature environment in summer, the air inlet device can be integrally stopped, and cold air is supplied to the pipeline workshop through air-conditioning refrigeration.
Example 4
In order to guarantee that the condensation dewatering device can carry out condensation dewatering to the high temperature waste gas of input wherein, provide following technical scheme about condensation dewatering device.
The condensation dewatering device comprises an outer sleeve 304 and a condensation cylinder 305 arranged on the top of the outer sleeve 304, a spiral wound spiral channel 306 is fixedly connected to the outer wall of the condensation cylinder 305, a second communicating pipe 302 is communicated with the top end of the inner side of the condensation cylinder 305, a first communicating pipe 205 is communicated with the middle section of the outer sleeve 304, a water supply pipe 301 is communicated with the bottom end of the inner side of the outer sleeve 304, a spiral condensing pipe 307 is fixedly connected to the inner wall of the condensation cylinder 305, and a refrigerant medium is filled in the spiral condensing pipe 307.
The high-temperature exhaust gas after combustion treatment in the combustion cylinder 201 is conveyed into the outer sleeve 304 through the first communication pipe 205, and spirally ascends through the spiral passage 306, and is sufficiently heat-exchanged with the refrigerant in the spiral condensing pipe 307 to condense the water vapor therein, the condensed water vapor can flow downwards through the spiral passage 306 and drip and collect to the bottom of the outer sleeve 304, and the water supply pipe 301 and the first pressure pump 303 matched therewith can convey the condensed water collected at the bottom of the outer sleeve 304 to the heating kettle 202 to supplement clean water to the heating kettle 202.
On the basis of the above technical solution regarding the condensation and water removal device, in order to ensure that the refrigerant medium in the spiral condensation pipe 307 continuously maintains a low temperature state, so as to cool the high temperature exhaust gas, and condense and collect the water vapor therein, the following technical solution is provided.
The condenser is further provided with a cooler 308, a refrigerant inlet of the cooler 308 is communicated with the bottom end of the spiral condenser pipe 307 through a refrigerant inlet pipe 309, a refrigerant outlet of the cooler 308 is communicated with the top end of the spiral condenser pipe 307 through a refrigerant outlet pipe 310, and a second pressure pump 311 is mounted on the refrigerant outlet pipe 310 in a matched manner.
Under the pressurization effect of the second pressurization pump 311, the refrigerant base which can cool the cooler 308 is conveyed to the top end of the spiral condensation pipe 307 from the refrigerant outlet, and flows downwards along the spiral condensation pipe 307, and the high-temperature hot gas entering the outer sleeve 304 flows upwards from bottom to top along the spiral passage 306, the high-temperature hot gas can be cooled under the heat exchange effect of the high-temperature hot gas and the refrigerant medium, the refrigerant medium with the increased temperature is input into the cooler 308 from the bottom of the spiral condensation pipe 307 through the refrigerant inlet pipe 309, and the recovered refrigerant medium is cooled again by the cooler 308, so that the circulating flow of the refrigerant medium is realized, and the high-temperature waste gas is further cooled continuously.
Due to the arrangement of the spiral channel 306, the retention time of the high-temperature exhaust gas at the periphery of the condensation cylinder 305 can be prolonged, and the cooling effect of the high-temperature exhaust gas is improved.
Example 5
For guaranteeing that adsorption equipment can handle the waste gas of inputing wherein to effectively adsorbing poisonous and harmful substance, guarantee that exhaust gas accords with the exhaust emission standard, provide following technical scheme about adsorption equipment.
The adsorption device comprises an adsorption cylinder 401 and a plurality of layers of adsorption discs 402 fixedly installed in the adsorption cylinder 401, the second communicating pipe 302 is communicated with the inner bottom of the adsorption cylinder 401, each layer of adsorption disc 402 is arranged on the upper side of the communicated part of the second communicating pipe 302 and the adsorption cylinder 401, an adsorption cavity 403 is formed in each layer of adsorption disc 402, vent holes communicated with the adsorption cavity 403 are formed in the upper surface and the lower surface of the adsorption disc 402, and granular activated carbon is added into the adsorption cavity 403.
Waste gas after condensation water trap handles gets into in the adsorption cylinder 401 and vertical upflow by second communicating pipe 302, after getting into the inboard absorption chamber 403 of each layer adsorption disc 402 through the air vent, with the effect of granule active carbon wherein, by granule active carbon with poisonous, harmful substance adsorption to wherein in the waste gas, the waste gas that the process adsorption disc 402 was handled reaches emission standard and is discharged by adsorption cylinder 401 top.
On the basis of the above technical scheme about the adsorption equipment, in order to ensure that each layer of adsorption disks 402 can be stably installed in the adsorption cylinder 401 and ensure that the exhaust gas subjected to adsorption treatment can be output from the adsorption cylinder 401, the following technical scheme is provided.
The inside wall rigid coupling of absorption section of thick bamboo 401 has multilayer collar 404, adsorbs dish 402 fixed mounting on collar 404, and the bottom intercommunication of absorption section of thick bamboo 401 has blast pipe 405, and blast pipe 405 sets up to the type of falling U.
The setting of collar 404 can cross and guarantee each layer adsorption disc 402 and stably install in adsorbing a section of thick bamboo 401, sets up blast pipe 405 into the type of falling U, can avoid external dust to follow blast pipe 405 and get into the adsorption performance who influences adsorption disc 402 and wherein granule active carbon in adsorbing a section of thick bamboo 401.
On above technical scheme basis about adsorption equipment, for avoiding leading to the granule active carbon to take place to bond because of carrying a small amount of steam by the waste gas of condensation water trap input, can effectively improve the adsorption efficiency of granule active carbon to poisonous and harmful substance simultaneously, provide following technical scheme.
Install the installation axle 406 of vertical arrangement in the absorption section of thick bamboo 401 in the rotation, and install the axle 406 and keep rotating with each group's adsorption disc 402 and be connected, fixed mounting has the multilayer stirring rake 407 of evenly arranging on the installation axle 406, and each layer stirring rake 407 arranges respectively in the absorption chamber 403 in each layer adsorption disc 402, and absorption section of thick bamboo 401 top still fixed mounting has driving motor 408, and driving motor 408 and installation axle 406 power is connected.
Drive installation axle 406 and stirring rake 407 rotation in-process on it at driving motor 408, can stir the granular activated carbon flow in each layer adsorption disc 402, can effectively avoid granular activated carbon to receive the vapor influence to take place to bond, and the granular activated carbon of stirring simultaneously can improve its and the contact surface of waste gas, improves its adsorption effect to poisonous and harmful substance.
In order to ensure that the driving motor 408 can drive the mounting shaft 406 to rotate stably, a driving gear is fixedly connected to a rotating shaft of the driving motor 408, a transmission gear is fixedly connected to the top end of the mounting shaft 406, the driving gear is meshed with the transmission gear, and the driving gear is driven to rotate when the driving motor 408 works, so that the transmission gear and the mounting shaft 406 are driven to rotate stably.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (10)
1. An air conditioning system for a pipeline production plant, characterized in that: the system comprises an air inlet device, a waste gas combustion device, a condensation dewatering device and an adsorption device, wherein the air inlet device comprises a mixing box (101), and a heat supply pipe (102), a normal temperature pipe (103) and an air inlet pipe (104) which are connected to the mixing box (101), the normal temperature pipe (103) and the heat supply pipe (102) are communicated with the external environment, the heat supply pipe (102) is connected with a spiral heating pipe (105) installed in the waste gas combustion device, and the air inlet pipe (104) is communicated to a pipeline production workshop; the waste gas combustion device comprises a combustion cylinder (201), a heating kettle (202) and an air supply disc (203), wherein the heating kettle (202) and the air supply disc (203) are arranged in an inner cavity of the combustion cylinder (201), the heating kettle (202) and the air supply disc (203) are respectively installed at the top and the bottom of the combustion cylinder (201), the air supply disc (203) is used for conveying waste gas collected in a pipeline production workshop to the combustion cylinder (201), an igniter (204) is also fixedly installed in the combustion cylinder (201) and is arranged above the air supply disc (203), the spiral heating pipe (105) is fixedly installed in the heating kettle (202), and the combustion cylinder (201) is communicated with a condensation and water removal device through a first communication pipe (205); the condensation dewatering device is communicated with the heating kettle (202) through a water supply pipe (301); the adsorption device is communicated with the cooling and water removing device through a second communicating pipe (302).
2. The air-conditioning system for a pipeline production plant according to claim 1, wherein: an air supply pipeline is arranged in the air supply disc (203), an exhaust gas spray head (206) communicated with the air supply pipeline is uniformly arranged on the upper surface of the air supply disc (203), the air supply pipeline in the air supply disc (203) is communicated with a pipeline workshop through an exhaust gas conveying pipe (207), and a first air supply pump (208) is installed on the exhaust gas conveying pipe (207) in a matched mode.
3. The air-conditioning system for a pipeline production plant according to claim 1, wherein: the heating system is characterized in that the heating pipe (102) comprises two sections fixedly connected with the heating kettle (202), two ends of the spiral heating pipe (105) are fixedly connected with the heating pipe (102) at two ends and are communicated, a second air supply pump (106) is installed on the heating pipe (102) in a matched mode, the water supply pipe (301) is communicated to the inner side of the top of the heating kettle (202), a first pressure pump (303) is installed on the water supply pipe (301) in a matched mode, and the top of the heating kettle (202) is further communicated with a pressure stabilizing pipe (210) and a water injection pipe (211).
4. The air-conditioning system of a pipeline production plant according to claim 1, wherein: the utility model discloses a heating kettle, including combustion cylinder (201), gas supply dish (203), heating kettle (202), gas supply dish (201) inner wall rigid coupling has lower floor's mounting ring (209), gas supply dish (203) fixed mounting is on lower floor's mounting ring (209), combustion cylinder (201) top outer wall rigid coupling has upper mounting ring (212), heating kettle (202) fixed mounting is on upper mounting ring (212).
5. The air-conditioning system of a pipeline production plant according to claim 1, wherein: all form a complete set and install electromagnetic flow valve (107) on normal atmospheric temperature pipe (103), heat supply pipe (102), still form a complete set and install third air feed pump (108) on normal atmospheric temperature pipe (103), heat supply pipe (102) and mixing box (101) intercommunication department fixed mounting have first temperature sensor, form a complete set and install fourth air feed pump (109) on intake pipe (104), and intake pipe (104) and mixing box (101) intercommunication department fixed mounting have the second temperature sensor.
6. The air-conditioning system of a pipeline production plant according to claim 1, wherein: the condensation dewatering device comprises an outer sleeve (304) and a condensation cylinder (305) arranged at the top of the outer sleeve (304), wherein a spiral channel (306) wound in a spiral mode is fixedly connected to the outer wall of the condensation cylinder (305), a second communicating pipe (302) is communicated with the top end of the inner side of the condensation cylinder (305), a first communicating pipe (205) is communicated to the middle section of the outer sleeve (304), a water supply pipe (301) is communicated with the bottom end of the inner side of the outer sleeve (304), a spiral condensing pipe (307) is fixedly connected to the inner wall of the condensation cylinder (305), and a refrigerant medium is filled in the spiral condensing pipe (307).
7. The air-conditioning system for a pipeline production plant according to claim 6, wherein: still be provided with cooler (308), the refrigerant import of cooler (308) advance pipe (309) through the refrigerant with spiral condenser pipe (307) bottom intercommunication, the refrigerant export of cooler (308) through refrigerant exit tube (310) with spiral condenser pipe (307) top intercommunication, and supporting second force (forcing) pump (311) of installing on refrigerant exit tube (310).
8. The air-conditioning system for a pipeline production plant according to claim 1, wherein: adsorption equipment includes an adsorption cylinder (401) and multilayer adsorption disc (402) of fixed mounting in adsorption cylinder (401), the second is communicating pipe (302) and the inboard bottom intercommunication of an adsorption cylinder (401), each layer adsorption disc (402) is arranged in the second top side of communicating pipe (302) and adsorption cylinder (401) intercommunication department, and has seted up in each layer adsorption disc (402) and has adsorbed chamber (403), the upper and lower surface of adsorption disc (402) all seted up with adsorb the air vent of chamber (403) intercommunication, it has the granule active carbon to add in adsorption chamber (403).
9. The air-conditioning system of a pipeline production plant according to claim 8, wherein: adsorb a section of thick bamboo (401) inside wall rigid coupling has multilayer collar (404), adsorb dish (402) fixed mounting on collar (404), it has blast pipe (405) to adsorb a section of thick bamboo (401) bottom intercommunication, and blast pipe (405) sets up to the type of falling U.
10. The air-conditioning system for a pipeline production plant according to claim 8, wherein: the adsorption cylinder (401) is rotatably provided with a vertically arranged installation shaft (406), the installation shaft (406) is rotatably connected with each group of adsorption discs (402), the installation shaft (406) is fixedly provided with a plurality of layers of uniformly arranged stirring paddles (407), each layer of stirring paddles (407) is respectively arranged in an adsorption cavity (403) of each layer of adsorption discs (402), the top of the adsorption cylinder (401) is also fixedly provided with a driving motor (408), and the driving motor (408) is in power connection with the installation shaft (406).
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| CN202211191287.1A CN115554804A (en) | 2022-09-28 | 2022-09-28 | Air conditioning system of pipeline production workshop |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117427489A (en) * | 2023-12-08 | 2024-01-23 | 汉寿潇汉新材料科技有限公司 | Waste gas treatment system in water-based paint production process |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201042697Y (en) * | 2007-04-17 | 2008-04-02 | 东莞泽龙线缆有限公司 | Hot wind exchange type stoving oven device |
| CN107062275A (en) * | 2017-05-22 | 2017-08-18 | 浙江长城电工科技股份有限公司 | A kind of enameling machine oven waste gas tail gas multi-processing methods and its device |
| CN207941313U (en) * | 2018-01-26 | 2018-10-09 | 山西美佳锦环保科技有限公司 | A kind of energy-saving and environment-friendly exhaust gas purification and treatment device |
| CN208287673U (en) * | 2018-05-03 | 2018-12-28 | 河北清大环保机械有限公司 | A kind of catalytic combustion system |
| CN208906568U (en) * | 2018-10-11 | 2019-05-28 | 东台市富安合成材料有限公司 | One kind compressing formula synthetic leather foam device |
| JP6552762B1 (en) * | 2019-03-28 | 2019-07-31 | 株式会社タクマ | Combined plant and excess heat recovery method for combined plant |
| CN209355713U (en) * | 2018-12-29 | 2019-09-06 | 江苏天祺环保科技有限公司 | A kind of circulation mechanism of high temperature oxidation furnace |
| CN212339620U (en) * | 2020-06-18 | 2021-01-12 | 北京祥晨建设有限公司 | Heating boiler convenient to circulate and wash |
| CN114471078A (en) * | 2022-01-27 | 2022-05-13 | 中国电力工程顾问集团西北电力设计院有限公司 | Temperature swing adsorption device and method for capturing carbon dioxide in flue gas for power plant |
-
2022
- 2022-09-28 CN CN202211191287.1A patent/CN115554804A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201042697Y (en) * | 2007-04-17 | 2008-04-02 | 东莞泽龙线缆有限公司 | Hot wind exchange type stoving oven device |
| CN107062275A (en) * | 2017-05-22 | 2017-08-18 | 浙江长城电工科技股份有限公司 | A kind of enameling machine oven waste gas tail gas multi-processing methods and its device |
| CN207941313U (en) * | 2018-01-26 | 2018-10-09 | 山西美佳锦环保科技有限公司 | A kind of energy-saving and environment-friendly exhaust gas purification and treatment device |
| CN208287673U (en) * | 2018-05-03 | 2018-12-28 | 河北清大环保机械有限公司 | A kind of catalytic combustion system |
| CN208906568U (en) * | 2018-10-11 | 2019-05-28 | 东台市富安合成材料有限公司 | One kind compressing formula synthetic leather foam device |
| CN209355713U (en) * | 2018-12-29 | 2019-09-06 | 江苏天祺环保科技有限公司 | A kind of circulation mechanism of high temperature oxidation furnace |
| JP6552762B1 (en) * | 2019-03-28 | 2019-07-31 | 株式会社タクマ | Combined plant and excess heat recovery method for combined plant |
| CN212339620U (en) * | 2020-06-18 | 2021-01-12 | 北京祥晨建设有限公司 | Heating boiler convenient to circulate and wash |
| CN114471078A (en) * | 2022-01-27 | 2022-05-13 | 中国电力工程顾问集团西北电力设计院有限公司 | Temperature swing adsorption device and method for capturing carbon dioxide in flue gas for power plant |
Non-Patent Citations (1)
| Title |
|---|
| （日）藤刚宏: "《氟利昂制冷机的原理和实践》", 航空工业出版社, pages: 184 - 185 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117427489A (en) * | 2023-12-08 | 2024-01-23 | 汉寿潇汉新材料科技有限公司 | Waste gas treatment system in water-based paint production process |
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Application publication date: 20230103 |