CN110255856A - Steam heat pump sludge drying system - Google Patents
Steam heat pump sludge drying system Download PDFInfo
- Publication number
- CN110255856A CN110255856A CN201910691185.8A CN201910691185A CN110255856A CN 110255856 A CN110255856 A CN 110255856A CN 201910691185 A CN201910691185 A CN 201910691185A CN 110255856 A CN110255856 A CN 110255856A
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- pipe
- salting liquid
- sludge
- absorption tower
- baking oven
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention provides a kind of steam heat pump sludge drying systems, including a sludge baking oven, an evaporator, a generator, an absorption tower, a preheater and a condenser；Sludge baking oven top and the evaporator pass through the first air line, the evaporator and the condenser pass through the second air line, second air hose is arranged across the preheater, and the bottom end of the condenser and the sludge baking oven passes through third air line；The evaporator is connected to the absorption tower by the first steam pipe, salting liquid is provided in the absorption tower, the absorption tower is connected to the preheater and respectively by the first salting liquid pipe, the first salting liquid return pipe, and the absorption tower passes through the second salting liquid pipe respectively with the generator and the second salting liquid return pipe is connected to.Installed power of the present invention is small, and operating cost is low, applied widely to energy utilization efficiency height, possesses good economic value and dissemination.
Description
Technical field
The present invention relates to industrial sludge Decrement Technique field, in particular to a kind of steam heat pump sludge drying system.
Background technique
As the continuous development of China's economy develops, the continuous propulsion of urbanization, the continuous improvement of sewage treatment capacity, dirt
Water process final product sludge quantity is also being continuously increased, it is contemplated that the only municipal sludge yield (moisture content 80%) in the year two thousand twenty China
It is up to 6000~90,000,000 tons.Sludge is a kind of to be made of extremely organic debris, inorganic particle, microorganism, colloid etc.
Complicated heterogeneous body stablizes processing in order to avoid secondary pollution must carry out deep dehydration to sludge.The density of population in China
Greatly, shortage of land resource, the extensive style processing method such as traditional landfill are difficult to continue progress, and the harmless treatment of sludge is disposed will
It is the priority and difficulty problem that environment protection field faces.Sludge incineration technology is to generally acknowledge most thorough method of disposal both at home and abroad, is biochemical
Sludge reduction, innoxious inevitable approach.Sludge calorific value before non-desiccation is reduced is lower, directly burns and needs to heat a large amount of combustions
Material causes burning operating cost higher, greatly hinders the popularization and application of burning process.Sewage sludge harmlessness disposing field at present
Need a kind of drying sludge technology that maturation is energy-efficient linking front and back segment process.
Summary of the invention
The present invention provides a kind of steam heat pump sludge drying systems, and its purpose is to solve existing electric heating pump sludge
Drying technique often faces that factory transformer capacity is insufficient and the situation of steam affluence in practical applications, and it is further to constrain it
The problem of popularization.
In order to achieve the above object, the present invention provides a kind of steam heat pump sludge drying system, including a sludge baking oven,
One evaporator, a generator, an absorption tower, a preheater and a condenser；
A wet mud feed inlet and a dry mud discharge port, the top of the sludge baking oven and institute are provided on the sludge baking oven
Evaporator is stated by the first air line, the evaporator and the condenser are by the second air line, and described second
Air hose is arranged across the preheater, and the bottom end of the condenser and the sludge baking oven passes through third air line；
The evaporator is connected to the absorption tower by the first steam pipe, and salting liquid, institute are provided in the absorption tower
Absorption tower is stated to be connected to the preheater and respectively by the first salting liquid pipe, the first salting liquid return pipe, the absorption tower with
The generator passes through the second salting liquid pipe and the connection of the second salting liquid return pipe respectively；
A high-temperature steam entrance is provided on the generator, the generator and the condenser pass through the second steam pipe
Connection, the condenser are connected to the evaporator by a condensate pipe.
Wherein, the transmission mesh belt of multilayer is provided in the sludge baking oven, the top of the sludge baking oven is provided with a collection
Device of air and a dust-extraction unit.
Wherein, it is additionally provided with water cooling plant, including a water cooler and a cooling tower on first air hose, described first
Air hose is arranged across the water cooler, and the cooler and the cooling tower pass through a cooling water pipe and a cooling water return pipe
Connection.
Wherein, a cooling water supply port is additionally provided on the cooling tower.
Wherein, a regenerator, the second salting liquid pipe and institute are additionally provided between the absorption tower and the generator
It states the second salting liquid return pipe and both passes through the regenerator setting.
Wherein, a spray equipment, the first salting liquid return pipe and second salt are additionally provided in the absorption tower
Solution backflow pipe is connect with the spray equipment.
Wherein, a condensation-water drain is provided on the water cooler, the evaporator and the generator.
It wherein, further include a blower, a cooling water pump, a circulating pump and a throttle valve, the blower setting is described the
On one air hose, between the sludge baking oven and the water cooler, the cooling water pump is arranged described cold the blower
But on water pipe, the junction of the first salting liquid pipe and the second salting liquid pipe is arranged in the circulating pump, and the throttle valve is set
It sets on the condensate pipe.
Above scheme of the invention have it is following the utility model has the advantages that
Steam heat pump sludge drying system of the invention, uses water as refrigerant, and dense saline solution is realized as absorbent
Energy recycles in sludge drying course, substantially increases steam utilization, in installed capacity restricted and steam is rich
Abundant sludge reduction field, installed power of the invention is small, and operating cost is low, applied widely to energy utilization efficiency height,
Possess good economic value and dissemination；
Steam heat pump sludge drying system of the invention has also recycled whole tails while recycling a large amount of tail gas heat quantities
Gas avoids tail gas and damages to environment, is environmentally-friendly sludge anhydration system.
Detailed description of the invention
Fig. 1 is overall structure of the invention and piping connection schematic diagram.
[description of symbols]
1- sludge baking oven；2- evaporator；3- generator；The absorption tower 4-；5- preheater；6- condenser；The wet mud feed inlet of 7-；
The dry mud discharge port of 8-；The first air hose of 9-；The second air hose of 10-；11- third air hose；The first steam pipe of 12-；The first salt of 13-
Solution conduit；14- the first salting liquid return pipe；15- the second salting liquid pipe；16- the second salting liquid return pipe；17- high-temperature steam enters
Mouthful；The second steam pipe of 18-；19- condensate pipe；20- is driven mesh belt；21- gas collecting apparatus；22- dust-extraction unit；23- water cooler；
24- cooling tower；25- cooling water pipe；26- cooling water return pipe；27- cooling water supply port；28- regenerator；29- spray equipment；
30- condensation-water drain；31- blower；32- cooling water pump；33- circulating pump；34- throttle valve.
Specific embodiment
To keep the technical problem to be solved in the present invention, technical solution and advantage clearer, below in conjunction with attached drawing and tool
Body embodiment is described in detail.
The present invention often faces factory's transformer capacity for existing electric heating pump sludge drying technique in practical applications
The insufficient and situation of steam affluence, provides a kind of steam heat pump sludge drying system at the problem of constraining its further genralrlization.
As shown in Figure 1, the embodiment provides a kind of steam heat pump sludge drying system, including a sludge baking oven
1, an evaporator 2, a generator 3, an absorption tower 4, a preheater 5 and a condenser 6；One is provided on the sludge baking oven 1
Wet mud feed inlet 7 and a dry mud discharge port 8, the top of the sludge baking oven 1 and the evaporator 2 are connected by the first air hose 9
Logical, the evaporator 2 is connected to the condenser 6 by the second air hose 10, and second air hose 10 passes through the preheating
Device 5 is arranged, and the condenser 6 is connected to the bottom end of the sludge baking oven 1 by third air hose 11；The evaporator 2 and institute
It states absorption tower 4 to be connected to by the first steam pipe 12, salting liquid, the absorption tower 4 and the preheating is provided in the absorption tower 4
Device 5 is connected to by the first salting liquid pipe 13, the first salting liquid return pipe 14 respectively, and the absorption tower 4 is distinguished with the generator 3
It is connected to by the second salting liquid pipe 15 with the second salting liquid return pipe 16；A high-temperature steam entrance is provided on the generator 3
17, the generator 3 is connected to the condenser 6 by the second steam pipe 18, and the condenser 6 passes through with the evaporator 2
The connection of one condensate pipe 19.
Steam heat pump sludge drying system described in the above embodiment of the present invention, the wet mud being arranged on sludge baking oven 1 into
Material mouth 7 and dry mud discharge port 8, wet mud feed inlet 7 are connected to a sludge molding machine, and molding sludge is imported in sludge baking oven 1, do
Mud discharge port 8 is connected to a Shaftless screw conveyor or scraper lifting machine, and does sealing thermal insulation processing at dry mud discharge port 8, leads to
Shaftless screw conveyor or scraper lifting machine is crossed to export the sludge of desiccation.Temperature is 90 DEG C or so by third air hose 11
Heated dry air, which is imported and swept upwards from the bottom end of sludge baking oven 1, blows sludge, and sludge drying belt is walked moisture, has absorbed water after the completion
The humid air divided is assembled on 1 top of sludge baking oven, and imports in the first air hose 9.Wherein, the desiccation temperature of entire sludge baking oven 1
Degree control is at 55 DEG C or so.It sweeps the humid air temperature after blowing and is similarly 55 DEG C or so, imported in evaporator 2 with the first air hose 9,
A finned heat exchanger is provided in evaporator 2, humid air flows through finned heat exchanger and is cooled under the action of condensed water
33 DEG C or so, cool-down dehumidification is completed, generates condensed water.Subsequent remaining air is imported again in the second air hose 10, by preheating
Dilute salting liquid preheating in device 5, using the finned heat exchanger being arranged in condenser 6, is further heated by medium temperature steam
To 90 DEG C or so, then continues to sweep sludge into sludge baking oven 1 by third air hose 11 and blow drying.
Temperature be 150 DEG C or so high-temperature steam by high-temperature steam entrance 17 enter generator 3 in, with dilute salting liquid into
Row heat exchange, dilute salting liquid evaporation generates 120 DEG C or so of medium temperature steam, then is imported in condenser 6 by the second steam pipe 18,
Heat exchange is completed with the air in condenser 6, is converted into condensed water, is then entered in evaporator 2 by condensate pipe 19, and it is wet
Air carries out heat exchange again, and humid air is cooled to 33 DEG C or so and is dehumidified.Condensed water is in evaporator 2 and humid air heat exchange
Afterwards, the Low Temperature Steam that heat of vaporization forms 30 DEG C or so is absorbed, then absorption tower 4 is entered by the first steam pipe 12, is absorbed tower 4
Interior dense saline solution absorbs.
Dense saline solution in absorption tower 4 generates 90 DEG C or so of dilute salting liquid after absorbing Low Temperature Steam, wherein a-road-through
It crosses the first salting liquid pipe 13 to enter in preheater 5, carries out heat exchange with the air in the second air hose 10, pre-add is carried out to air
Heat.Temperature is down to 70 DEG C or so to dilute salting liquid after the heat exchange, is back in absorption tower 4 by the first salting liquid return pipe 14.
Meanwhile another way dilute salting liquid is flowed into generator 3 by the second salting liquid pipe 15, carries out heat with 150 DEG C or so high-temperature steams
Exchange, 120 DEG C or so of medium temperature steam and dense saline solution are generated by evaporation, and subsequent dense saline solution passes through the second salting liquid
Return pipe 16 is back in generator 3, is completed salting liquid all the way and is recycled.
Wherein, the transmission mesh belt 20 of multilayer is provided in the sludge baking oven 1, the top of the sludge baking oven 1 is provided with
One gas collecting apparatus 21 and a dust-extraction unit 22.It is driven settable three to four layers of mesh belt 20, the movement between adjacent drive mesh belt 20
It is contrary so that distance that heated dry air flows in sludge baking oven 1 and the area contacted with sludge are bigger, drying efficiency and
Better effect.The clammy collect air for absorbing moisture in the apical position of sludge baking oven 1, is passed through plate-type dedusting by gas collecting apparatus 21
The dust-extraction units such as device or bag filter 22 remove the tiny mud granule in clammy air, prevent it from entering pipe-line system
It is interior.
Wherein, water cooling plant, including a water cooler 23 and a cooling tower 24, institute are additionally provided on first air hose 9
It states the first air hose 9 to be arranged across the water cooler 23, the cooler 23 and the cooling tower 24 pass through a cooling water pipe 25
It is connected to a cooling water return pipe 26.A cooling water supply port 27 is additionally provided on the cooling tower 24.In first air hose 9
Humid air will first pass through water cooler 23 before entering evaporator 2, and the pre- cooling of completion is exchanged with cooling water heat.Wherein in water cooler 23
It is provided with finned heat exchanger, water cooler 23 is connected to cooling tower 24, and the cooling water in cooling tower 24 is flowed by cooling water pipe 25
The finned heat exchanger surface for entering water cooler 23 is then back to humid air cool-down dehumidification by cooling water return pipe 26 again
Cooling tower 24.In addition, cooling water can be supplemented into cooling tower 24 by cooling water supply port 27, it is ensured that it can be cyclically to first
Humid air cool-down dehumidification in air hose 9.
Wherein, a regenerator 28, the second salting liquid pipe are additionally provided between the absorption tower 4 and the generator 3
15 and the second salting liquid return pipe 16 both pass through the regenerator 28 and be arranged.90 DEG C or so of dilute salting liquid enters generator
Regenerator 28 will be flowed through before 3,100 DEG C or so is preheated to by regenerator 28, enters back into generator 3, with 150 DEG C or so
High-temperature steam carries out heat exchange, generates 120 DEG C or so of dense saline solution, then flow through regenerator by the second salting liquid return pipe 16
28, the reversed convection current of dilute salting liquid with 90 DEG C or so carries out heat exchange, forms 100 DEG C or so of dense saline solution.Finally with first
70 DEG C or so of dilute salting liquid mixing, generates 80 DEG C or so of mixing salt solution in salting liquid return pipe 14.
Wherein, a spray equipment 29, the first salting liquid return pipe 14 and described are additionally provided in the absorption tower 4
Disalt solution backflow pipe 16 is connect with the spray equipment 29.100 DEG C or so of dense saline solution and 70 DEG C or so of dilute salt are molten
Liquid passes through the second salting liquid return pipe 16 respectively and the first salting liquid return pipe 14 flows into spray equipment 29, in spray equipment 29
Mixing generates 80 DEG C or so of mixing salt solution, and mixing salt solution is uniformly sprayed to absorption tower 4 finally by spray equipment 29
It is interior, it is sufficiently mixed with Low Temperature Steam, regenerates 90 DEG C or so of dilute salting liquid, form the circulation of salting liquid.The present invention passes through
Salting liquid, as refrigerant, realizes recycling for energy in sludge drying course, improves significantly as absorbent, water
The utilization rate of steam.
Wherein, a condensation-water drain 30 is provided on the water cooler 23, the evaporator 2 and the generator 3.Water
For humid air in cooler 23 under the heat exchange action of cooling water, the partial moisture in air generates condensed water, passes through water cooler
Condensation-water drain 30 on 23 is discharged.Humid air in evaporator 2 under the heat exchange action of condensed water, drops in condensate pipe 19
Temperature simultaneously further dehumidifies, and the condensed water that the partial moisture condensation in air generates will be by the condensation-water drain 30 on evaporator 2
Discharge.And the high-temperature steam in generator 3, after heat exchange occurs with dilute salting liquid, generate medium temperature steam and a certain amount of condensation
Water is discharged by the condensation-water drain 30 on generator 3.A heating coil wherein is set inside generator 3, is steamed respectively with high temperature
Vapour entrance 17 is connected with condensation-water drain 30, and high-temperature steam walks tube side, and salting liquid walks the shell of generator.
Wherein, the steam heat pump sludge drying system further includes a blower 31, a cooling water pump 32,33 and of a circulating pump
One throttle valve 34, the blower 31 are arranged on first air hose 9, and the blower 31 is located at the sludge baking oven 1 and institute
It states between water cooler 23, the first air hose of outlet 10 of blower 31 is connected with the windward side of water cooler 23, is made by blower 31
With driving humid air guiding water cooler 23 and following cycle system；The cooling water pump 32 is arranged on the cooling water pipe 25,
Driving cooling water recycles between water cooler 23 and cooling tower 24, takes away heat；The circulating pump 33 is arranged in first salt
The junction of solution conduit 13 and the second salting liquid pipe 15, for the dilute salting liquid in absorption tower 4 to be directed respectively into preheating by two-way
In device 5 and generator 3；The throttle valve 34 is arranged on the condensate pipe 19, for adjusting high and low nip pressure, controls
Condensate flow in condensate pipe 19, wherein evaporator 2 and absorption tower 4 are in low-pressure area, and generator 3 and condenser 6 are in
Higher-pressure region.
Wherein, using conventional high-temperature belt-type drying machine, 80% water content sludge desiccation per ton is to 20% hereinafter, needing 1.2
Ton steam, the exhaust gas formed after desiccation (including a large amount of vapor) discharge, serious heat loss after processing.And the present invention due to
Recycled the heat (being mainly derived from vapor) in a large amount of tail gas, 40% or so original steam usage amount can be saved, i.e., on
It states under kindred circumstances, 1 ton of sludge drying need to only use 0.72 ton of steam, it is assumed that the daily 100 tons of sludge of sewage treatment plant needs desiccation,
17520 tons of steam can be then saved every year, and steam price temporarily based on 240 yuan/ton, then can save 4,200,000 yuan, obvious energy conservation every year.
In addition the present invention has also recycled whole tail gas while recycling a large amount of tail gas heat quantities, avoids injury of the tail gas to environment.
The above is a preferred embodiment of the present invention, it is noted that for those skilled in the art
For, without departing from the principles of the present invention, it can also make several improvements and retouch, these improvements and modifications
It should be regarded as protection scope of the present invention.
Claims (8)
1. a kind of steam heat pump sludge drying system, which is characterized in that including a sludge baking oven, an evaporator, a generator, one
Absorption tower, a preheater and a condenser；
A wet mud feed inlet and a dry mud discharge port, the top of the sludge baking oven and the steaming are provided on the sludge baking oven
It sends out device and the second air line, second air is passed through by the first air line, the evaporator and the condenser
Pipe is arranged across the preheater, and the bottom end of the condenser and the sludge baking oven passes through third air line；
The evaporator is connected to the absorption tower by the first steam pipe, and salting liquid, the suction are provided in the absorption tower
Receive tower be connected to the preheater and respectively by the first salting liquid pipe, the first salting liquid return pipe, the absorption tower with it is described
Generator passes through the second salting liquid pipe and the connection of the second salting liquid return pipe respectively；
A high-temperature steam entrance, the generator and the condenser is provided on the generator to connect by the second steam pipe
Logical, the condenser is connected to the evaporator by a condensate pipe.
2. steam heat pump sludge drying system according to claim 1, which is characterized in that be provided in the sludge baking oven
The top of the transmission mesh belt of multilayer, the sludge baking oven is provided with a gas collecting apparatus and a dust-extraction unit.
3. steam heat pump sludge drying system according to claim 1, which is characterized in that also set on first air hose
It is equipped with water cooling plant, including a water cooler and a cooling tower, first air hose is arranged across the water cooler, the cooling
Device is connected to the cooling tower by a cooling water pipe and a cooling water return pipe.
4. steam heat pump sludge drying system according to claim 3, which is characterized in that be additionally provided on the cooling tower
One cooling water supply port.
5. steam heat pump sludge drying system according to claim 1, which is characterized in that the absorption tower and the generation
A regenerator is additionally provided between device, the second salting liquid pipe and the second salting liquid return pipe both pass through the regenerator
Setting.
6. steam heat pump sludge drying system according to claim 5, which is characterized in that be additionally provided in the absorption tower
One spray equipment, the first salting liquid return pipe and the second salting liquid return pipe are connect with the spray equipment.
7. steam heat pump sludge drying system according to claim 3, which is characterized in that the water cooler, the evaporation
A condensation-water drain is provided on device and the generator.
8. steam heat pump sludge drying system according to claim 3, which is characterized in that further include a blower, a cooling
Water pump, a circulating pump and a throttle valve, the blower are arranged on first air hose, and the blower is located at sludge baking
Between case and the water cooler, the cooling water pump is arranged on the cooling water pipe, and the circulating pump is arranged described first
The junction of salting liquid pipe and the second salting liquid pipe, the throttle valve are arranged on the condensate pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910691185.8A CN110255856A (en) | 2019-07-29 | 2019-07-29 | Steam heat pump sludge drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910691185.8A CN110255856A (en) | 2019-07-29 | 2019-07-29 | Steam heat pump sludge drying system |
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| Publication Number | Publication Date |
|---|---|
| CN110255856A true CN110255856A (en) | 2019-09-20 |
Family
ID=67912276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910691185.8A Pending CN110255856A (en) | 2019-07-29 | 2019-07-29 | Steam heat pump sludge drying system |
Country Status (1)
| Country | Link |
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| CN (1) | CN110255856A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110550847A (en) * | 2019-10-18 | 2019-12-10 | 湖南清源华建环境科技有限公司 | Energy-saving heat pump sludge drying system |
| CN110563306A (en) * | 2019-10-18 | 2019-12-13 | 湖南清源智造设备有限公司 | Multiphase dehumidification sludge drying system |
| CN111453968A (en) * | 2020-04-08 | 2020-07-28 | 湖南清源智造设备有限公司 | Sludge drying and incineration coupling treatment system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2979423A1 (en) * | 2008-02-15 | 2013-03-01 | Egis Eau | SOLAR DRYING GLASS WITH HEATED FLOOR HEATED THROUGH SOLAR ENERGY |
| CN108164120A (en) * | 2018-01-24 | 2018-06-15 | 广州研华环境科技有限公司 | A kind of sludge drier |
| CN208776555U (en) * | 2018-12-10 | 2019-04-23 | 云南宁茂环境科技有限公司 | A kind of efficient dehumidification device of sludge |
| CN109956646A (en) * | 2019-04-03 | 2019-07-02 | 河南小威环境科技有限公司 | A kind of sludge drying treatment system |
| CN110040934A (en) * | 2019-04-19 | 2019-07-23 | 松下制冷（大连）有限公司 | A kind of sludge drying dehumidification system and method based on absorption heat pump |
-
2019
- 2019-07-29 CN CN201910691185.8A patent/CN110255856A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2979423A1 (en) * | 2008-02-15 | 2013-03-01 | Egis Eau | SOLAR DRYING GLASS WITH HEATED FLOOR HEATED THROUGH SOLAR ENERGY |
| CN108164120A (en) * | 2018-01-24 | 2018-06-15 | 广州研华环境科技有限公司 | A kind of sludge drier |
| CN208776555U (en) * | 2018-12-10 | 2019-04-23 | 云南宁茂环境科技有限公司 | A kind of efficient dehumidification device of sludge |
| CN109956646A (en) * | 2019-04-03 | 2019-07-02 | 河南小威环境科技有限公司 | A kind of sludge drying treatment system |
| CN110040934A (en) * | 2019-04-19 | 2019-07-23 | 松下制冷（大连）有限公司 | A kind of sludge drying dehumidification system and method based on absorption heat pump |
Non-Patent Citations (1)
| Title |
|---|
| 钟晓晖等: "《吸收式热泵技术及应用》", 30 September 2014, 冶金工业出版社 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110550847A (en) * | 2019-10-18 | 2019-12-10 | 湖南清源华建环境科技有限公司 | Energy-saving heat pump sludge drying system |
| CN110563306A (en) * | 2019-10-18 | 2019-12-13 | 湖南清源智造设备有限公司 | Multiphase dehumidification sludge drying system |
| CN111453968A (en) * | 2020-04-08 | 2020-07-28 | 湖南清源智造设备有限公司 | Sludge drying and incineration coupling treatment system |
| CN111453968B (en) * | 2020-04-08 | 2022-07-01 | 湖南清源智造设备有限公司 | Sludge drying and incineration coupling treatment system |
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Effective date of registration: 20190927 Address after: 410000 Room 107, Building A, Lugu Science and Technology Innovation Pioneering Park, 1698 Lugu West Avenue, Changsha High-tech Development Zone, Changsha City, Hunan Province Applicant after: Hunan Qingyuan Huajian Environmental Technology Co., Ltd. Address before: 410000 No. 2 Workshop of Hunan Academy of Nonferrous Metals Co., Ltd. No. 339 Wangcheng Avenue, Wangcheng Economic and Technological Development Zone, Changsha City, Hunan Province Applicant before: Hunan Qingyuan Intelligent Manufacturing Equipment Co., Ltd. |
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Application publication date: 20190920 |
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