CN206385089U - A kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal - Google Patents
A kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal Download PDFInfo
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- CN206385089U CN206385089U CN201621490665.6U CN201621490665U CN206385089U CN 206385089 U CN206385089 U CN 206385089U CN 201621490665 U CN201621490665 U CN 201621490665U CN 206385089 U CN206385089 U CN 206385089U
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Abstract
The utility model discloses a kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal, including is sequentially connected：Spraying cooling pipe, the spraying cooling for high-temperature gas mixture；Scrubber condenser, is further cooled down, acid-base neutralization and demisting to the high-temperature gas mixture being passed through, and obtains impure oil water mixture and rich gas；Automatic filter, for being filtered to described oil water mixture；Oil water separator, for the oil water mixture after separating and filtering and obtains bio oil and waste water.The utility model to the high-temperature oil gas refrigerated separation that charcoal processed is produced by obtaining bio oil, rich gas etc.；Carrying out combustion heat supplying to obtained rich gas is used for reactor gasification installation, and bio oil is used for heat supply or sale, realizes the recycling of organic solid castoff, recycles.
Description
Technical field
The utility model is related to field of solid waste treatment, more particularly to a kind of production of organic solid castoff charcoal
Raw high-temperature oil gas refrigerated separation device.
Background technology
With the development of the social economy, the protection and the promotion of green circulation economy of human ecological environment, discarded object are sharp again
With as the hot topic handled instantly, scientist will carry out the energy under anaerobic state using organic solid castoff as raw material to it
Change the method for processing, discarded object handled using Non-oxygen pyrolytic method, it is to avoid castoff burning or landfill pollution on the environment,
It is solid waste resource recovery, innoxious, environmental protection treatment good method.It is pyrolyzed a kind of carbonaceous material formed and is referred to as " biology
Charcoal ", charcoal is a kind of form of charcoal, can for a long time be stored in without being broken down into carbon dioxide in soil, bury to after underground
Can there are hundreds of will not disappear to more than one thousand years.
It is one of study hotspot of field of renewable energy that organic solid castoff energy conversion, which is utilized,.It is main to include dirt
Mud, agriculture and forestry organic waste material, kitchen garbage and rubbish from cooking etc..Biological carbon can be present in nature steadily in the long term, with holding
The infertile field fertile soil of long property, promotes Soil Microorganism breeding, promotes plant growth, to carbon dioxide absorption, make dioxy in air
Change the function of carbon reduction；Biological carbon is rich in micropore, can not only supplement the content of organics of soil, can also improve the saturating of soil
Gas and drainage, moisture needed for accumulation plant root effectively preserve moisture and nutriment, increase soil fertility；Biological carbon exists
The special performance that agriculture field has, makes it during implementation of China " fertile soil engineering ", plays important, irreplaceable
Effect.
The current domestic processing method of disposal for sludge mainly has landfill, burning, land use, anaerobic digestion, heating
Desiccation and plus alkali stabilization.Sludge landfill takes a large amount of soils, and the effusion of generation is gentle to know from experience severe contamination underground water and air.
Due to containing pathogen, parasitic ovum, heavy metal and a variety of biodegradable organic compoundses in sludge during land use, into farmland
As the fertilizer of crops, it will be detrimental to health by food chain and animal and plant growth.Burning be realize sewage sludge harmlessness,
Minimizing, the most thoroughly method is stabilized, shared ratio is improved year by year in specific resistance to filtration, it has also become developed country
The major technique of use, but its technology and equipment investment is big, and operating cost is high, and high-temperature flue gas heat utilization efficiency is not high, domestic sludge
Burning also has increased trend year by year, but vent gas treatment and technique also have and improves and solve, and resident complains more, causes into postponing
Slowly.Some resource technologies that recent years occurs are also because processing cost is too high, and some technologies are still in laboratory research rank
Section, is difficult to large-scale promotion application in actual production.
Publication No. CN105601075A Chinese patent disclose a kind of pyrolyzing sludge carbonization treatment process and
Its device, sludge is squeezed through squeezer, pulverizer is crushed, mixing and blending machine is puddled, dry in interior heating rotary kiln drying machine after
After sending into storage bin in feeding pyrolysis carbide furnace；Pyrolysis carbonization occurs in pyrolysis carbide furnace for sludge, product solid carbon it is mixed
Outside compound output system, product vapor, pyrolysis gas, which enter, to be separated in separating-purifying tower, is purified；Combustible gas after purification
Send into burning in burner and convey thermal source for interior heating rotary kiln drying machine, the restructuring that purification ＆ isolation goes out is distributed to mixing and blending machine
The secondary pyrolysis of progress is puddled with sludge；The flue gas that heating furnace is produced, which is expelled in hot-blast stove, carries out secondary ablation；Whole device is produced
Outlet I of the raw tail gas through interior heating rotary kiln drying machine is discharged, after treatment qualified discharge.Although there is provided a whole day work
Skill flow and device, but separating-purifying equipment is relatively easy, it is difficult to the impurity of oil gas and the inside can just be separated by an equipment,
And the bio oil produced is also without further purification separation, so as to cause the cheap of product, it is impossible to embody its value.
Utility model content
It can not be disposed to reduce increasing organic solid castoff, enable organic solid castoff preferably resource
Change, minimizing, innoxious and stabilisation is utilized, and the utility model provides a kind of high temperature of organic solid castoff charcoal
Oil gas refrigerated separation device, is mainly separated into rich gas at normal temperatures by high-temperature oil gas by equipment such as refrigerated separation devices, raw
Thing oil, waste water etc..
The utility model uses concrete technical scheme as follows：
A kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal, including be sequentially connected：Spray is cold
But manage, the spraying cooling for high-temperature gas mixture；Scrubber condenser, is further cooled down to the high-temperature gas mixture being passed through, in soda acid
With and demisting, obtain impure oil water mixture and rich gas；Automatic filter, for described oil water mixture progress
Filtering；Oil water separator, for the oil water mixture after separating and filtering and obtains bio oil and waste water.
Wherein, the top of the scrubber condenser is connected with gas purifier by pipeline, and net for receiving gas
Change at least one surge tank that device discharges gas.
It is preferred that, the scrubber condenser is connected with acid-base neutralization circulation line, and sets the alkali lye of access circulation line
Groove and measuring pump.
It is further into scrubber condenser after high-temperature gas mixture is by spraying cooling pipe spraying cooling in the utility model
Cooling, acid-base neutralization, demisting obtains the oil water mixture and rich gas of certain impurity；By the oil water mixture pump of scrubber condenser
Mud and oil water mixture are obtained after automatic filter is filtered, oil water mixture is separated into oil water separator, given birth to
Thing oil and waste water；The rich gas of scrubber condenser is evolved with roots blower by gas purifier, into surge tank, by purification
Rich gas go heating furnace gas burner heat supply；The oil water mixture of scrubber condenser continuously plays circulation by water pump, surveys
Measure the alkali lye inside its acid-base property, lye tank (vat) and its acid-base property is adjusted with measuring pump；Waste water after oil water separator separation passes through water
Cooler heat exchange cooling, spraying cooling pipe spray is squeezed into water pump.The external circulating water cooling system of water cooler, passes through booster pump
Work.
Described spraying cooling pipe is obliquely installed, provided with multi-stage spray spray, and high-temperature gas mixture enters spraying cooling pipe, leads to
The heat that substantial amounts of spray liquid absorbs high-temperature gas mixture is crossed, high-temperature gas mixture temperature certain temperature is down to, making to coagulate has unit
Divide with water recovery into liquid, while the acidic materials of neutralized reaction product, protect follow-up equipment, and make by spray washing
With the acid ingredients such as dust and SO2, NOX in on-condensible gas can effectively being removed, favorably with the burning of follow-up fixed gas and subtracting
Few exhaust emission generation.
As preferential, the spray assembly in spraying cooling pipe is generally 5~10.The multistage spray that spraying cooling pipe is installed
The pressure gauge and thermometer of remote control and field control are installed, the oil water mixture temperature below scrubber condenser on mist
During rising, the pressure sprayed on spray refrigerator pipe is increased, while multiple sprayers are opened, until slowly reducing scrubber condenser oil
The temperature of aqueous mixtures；Conversely, when the oil water mixture temperature below scrubber condenser is too low, it is possible to decrease pressure, spray is closed
Mist, mitigates the pressure of oil water separator below.
Described scrubber condenser, the oily waste water and fixed gas that spraying cooling pipe comes out enters scrubber condenser, passes through
Packing layer improves the mass transfer of gas-liquid, heat exchange, and the temperature of fixed gas further is down into technological requirement, and raising can coagulate organic component
Condensation effect, strengthens the assimilation effect of the acid ingredients such as the dust removing effects and SO2, NOX of fixed gas, and top exit is filled provided with demisting
Put, reduce fixed gas band liquid.
As preferential, scrubber condenser top is provided with demister and sprayer unit, and centre is provided with packing layer, filler
Thickness degree is generally the 1/2~1/5 of scrubber condenser height；Internal oil water mixture pH value control is in 5~9, chilling temperature control
System is at 20~60 DEG C.
The oil water mixture of scrubber condenser bottom has the pressure gauge of remote control and field control, thermometer and pH meter,
When pH meter show value is less than requiring, measuring pump is opened, and the alkali lye inside lye tank (vat) is squeezed into and mixed always in the profit of circulation
Compound pipeline, when pH meter reaches requirement, measuring pump is stopped.
Alkali lye inside lye tank (vat) can use sodium hydroxide, potassium hydroxide etc., be generally available sodium hydroxide, price material benefit.
Described automatic filter, the oily waste water pumping of scrubber condenser lower storage is to automatic filter, and together
When the pH value of waste water is automatically adjusted by automatic feeding alkali lye before pump, automatic filter is Full-automatic liquid scraper filter, liquid
Body is flowed into from filter inlet, is flowed from up to down, is flowed to and is exported through cartridge surface；When cartridge surface be collected into it is a certain amount of
During impurity, the scraper of motor driving assembling adjuster is close to cartridge surface rotation, scrapes the removal of impurity, impurity is gathered in descending liquid
Collecting chamber, when a certain amount of impurity is arrived in accumulation, automatic blowdown valve opens collecting chamber, and the liquid containing high concentration impurities is discharged, row
Go out raffinate and reenter the processing of reactor high temperature cabonization.
Described gas purifier is also gas-liquid coalescing separator, a small amount of liquid and water mainly acted in separation gas
Mist, lubricant component, using multilayer is hydrophobic, oleophobic properties complex fiber material Coalescence filter core.
Described oil water separator, provided with internal structures such as entrance anti whip device, distribution wave resistance baffle plate, efficient coalescing-plates
Part, the waste water of automatic filter discharge enters oil water separator, effectively can quickly realize water-oil separating, the oil slick of collection is used as production
Thing is evacuated to oil storage tank automatically, and the waste water after oil removing is largely recycled as spray liquid, and redundance drains into sewage and set automatically
Apply processing.
As preferential, efficiently coalesce plate material and use DTS coalescing-plates filler (also known as the coalescent pack of bipyramid parallel-plate), melt
Current Conventional plate-type oil removing and coarse coalescence technology have been closed, has been a kind of high-efficiency liquid-liquid coarse separation filler, DTS coalescing-plates are filled out
Material is by a series of continuous 45 ° biconial plates up and down, by certain gap neat rule arranged in parallel up and down
Whole coalescent pack, it has the function and characteristic for greatly shortening the sinking time of the floating interval of floating dock and greasy filth of oil droplet, solid.Often
Individual upward bellmouth is oil outlet, and each downward bellmouth is mud hole, and coarse grain is distributed with per a piece of biconial plate bottom surface
Change salient point, when oil-polluted water is by DTS coalescing-plate fillers, these coarse salient points can catch very small oil droplet, pass through
45 ° of upward taper surfaces make oil droplet change from small to big, and complete local oil droplet coalescence, so as to be easier coalescence under buoyancy
Oil droplet is floated on the water surface from upward bellmouth.Equally, 45 ° of DTS coalescing-plates filler are designed to inferior pyramidal slag-drip opening, make to gather
Greasy filth and solid suspension after knot sink because of gravity, are coalesced by optic panel in downward taper recess and fall into bottom
Separator settling zone, this design is very beneficial for the separation of greasy filth floccule and solid, it is therefore prevented that coalescing-plate filler it is stifled
Plug, the fluid higher to viscous crude and solids content has extraordinary adaptability.It has treatment effeciency it is high, applied widely,
The features such as easy cleaning, easy care, installation operation are convenient, parallel-plate structure is arranged, separative efficiency is up to 99%.
As preferential, obtained waste water is transferred to sewage treatment plant through oil removal after air-flotation process.
Further preferential, obtained bio oil predominantly pyrolkigneous liquid, tar etc., density is larger, through precipitation, filters, point
From rear, oil burning apparatus is squeezed into by oil pump, can also squeeze into and be sold outside biological oil tank.
The hydrogen that described rich gas produces for organic solid castoff Pintsch process and after cooling down, carbon monoxide, methane etc.
More difficult compressed gas.By roots blower, gas purifier, the device such as surge tank, into the burning of gas burner device for
Answer gasification installation institute calorific requirement.
As preferential, surge tank is connected with liquid packing, and Stress control is in 0~60kpa.Surge tank is one or many
Individual, volume is 5m3~20m3。
Liquid packing is provided with the water seal height inside liquid level gauge, display, and water seal general action is in normal pressure tank, main function
Gas is prevented to be directly discharged to air, general gas flow is not toxic gas, but the gas with certain smell.Winter it is noted that
Water seal, which freezes, to be caused normally to show, pressure tank rises and can not emptied.
Buffering pot bottom is provided with liquid level gauge, when hydrops is arranged at bottom, by water pump discharge opeing, squeezes into sewage plant.
Described water cooler, purpose is reused after the waste water of circulated sprinkling is first passed through cooling.
As preferential, detachable plate heat exchanger can be used to enter water-filling-water heat exchange cooling, dismountable plate type for water cooler
Heat exchanger is a kind of new energy conserving heat exchanging device, small, easy to operate with heat-transfer effect height, compact conformation, floor space,
Cleaning, dismounting, easy to maintenance, the advantages of easily changing heat exchange area or path combination.Plate type heat exchanger is that had by a series of
A kind of new type high efficient heat exchanger of the sheet metal closed assembly of certain bellows-shaped.Thin rectangular shape passage is formed between various plates,
Heat exchange is carried out by half.Plate type heat exchanger is liquid-liquid, the ideal equipment of liquid-vapour progress heat exchange.Damaged in uniform pressure
In the case of mistake, its ratio of heat transfer coefficient pipe heat exchanger is high 3~5 times, and floor space is 1/3rd of pipe heat exchanger, recuperation of heat
Rate may be up to more than 90%.
Metal is fitted with before and after described water pump, booster pump, measuring pump and roots blower etc. to be flexible coupling, metal is flexible coupling
As a kind of flexible pressure-resistant pipe fitting, to compensate pipeline or machine, the mutual displacement of equipment connection end, vibrational energy, energy are absorbed
The effect such as vibration damping, noise reduction is enough played, with the multinomial feature such as flexible, light weight, corrosion-resistant, antifatigue, high-low temperature resistant, to set
It is standby preferably to be run under vibrations, corrosive atmosphere.
It is convenient for maintenance, maintenance can be set in the bottom of scrubber condenser, the upper end of oil water separator, the side of surge tank
Mouthful, maintenance door is sealed with access hole, when device breaks down, site operation personnel can be by access hole in device
Part repaired, maintenance door is closed after the completion of maintenance；The position that access hole is set can be determined according to practical matter.
The utility model is divided by the high-temperature oil gas cooling produced to organic solid castoff, especially sludge charcoal
From obtaining bio oil, rich gas etc..The wooden vinegar that combustion heat supplying is used in reactor gasification installation, bio oil is carried out to obtained rich gas
Liquid as being sold outside a kind of good liquid fertilizer, bio oil also can oneself heat supply, it is also commercially available to take out, be truly realized organic solid
The recycling of body discarded object, minimizing, innoxious and stabilisation turns waste into wealth, recycled.
Brief description of the drawings
Fig. 1 is the utility model high temperature oil gas refrigerated separation schematic device；
Fig. 2 is DTS coalescing-plate filler schematic diagrams.
Embodiment
High-temperature oil gas refrigerated separation device as illustrated in fig. 1 and 2, including it is sequentially connected spraying cooling pipe 1, scrubber condenser
2nd, automatic filter 3 and oil water separator 4.
Spraying cooling pipe 1 is obliquely installed, provided with 5~10 grades of spray assemblies 15, and high-temperature gas mixture A enters spraying cooling pipe,
The heat of high-temperature gas mixture is absorbed by substantial amounts of spray liquid, high-temperature gas mixture temperature is down to certain temperature, makes to coagulate organic
Component and water recovery are into liquid, while the acidic materials of neutralized reaction product.Remote control is installed on spraying spray assemblies 15
With the pressure gauge and thermometer of field control.
The top of scrubber condenser 2 is provided with demister 16 and sprayer unit 17, and centre is provided with packing layer 18, packing layer 18
Thickness is generally the 1/2~1/5 of scrubber condenser height；Internal oil water mixture pH value control is in 5~9, chilling temperature control
At 20~60 DEG C.
The oil water mixture of the bottom of scrubber condenser 2 has the pressure gauge of remote control and field control, thermometer and pH meter,
When pH meter show value is less than requiring, measuring pump 13 is opened, and the alkali lye of the inside of lye tank (vat) 10 is squeezed into oil always in circulation
Aqueous mixtures pipeline 19, when pH meter reaches requirement, measuring pump is stopped.
The oily waste water pumping of the lower storage of scrubber condenser 2 is to automatic filter 3, and simultaneously by being thrown automatically before pump
Plus alkali lye automatically adjusts the pH value of waste water, automatic filter 3 is Full-automatic liquid scraper filter, and liquid is from filter inlet stream
Enter, flow from up to down, flow to and export through cartridge surface；Cross filtering medium and be gathered in collecting chamber with descending liquid, when accumulation to one
During quantitative impurity, automatic blowdown valve opens collecting chamber, and the liquid containing high concentration impurities is discharged, and discharge raffinate reenters reaction
The processing of kettle high temperature cabonization.
Provided with internals such as entrance anti whip device, distribution wave resistance baffle plate, efficient coalescing-plates in oil water separator 4, from
The waste water of dynamic filter discharge enters oil water separator 4, effectively can quickly realize water-oil separating, the oil slick of collection as product from
Dynamic to be evacuated to oil storage tank, the waste water after oil removing is largely recycled as spray liquid, and redundance is drained at wastewater treatment facility automatically
Reason.
In the present embodiment, efficiently coalescence plate material uses DTS coalescing-plates filler (also known as the coalescent pack of bipyramid parallel-plate), such as
Shown in Fig. 2, fusion Conventional plate-type oil removing and coarse coalescence technology are a kind of high-efficiency liquid-liquid coarse separation filler, DTS coalescences
Plate filler is, by a series of continuous 45 ° biconial plates up and down, arranged in parallel to be formed by certain gap is neat up and down
Regular coalescent pack, it has the function that greatly shortens the sinking time of the floating interval of floating dock and greasy filth of oil droplet, solid and spy
Property.Each upward bellmouth is oil outlet, and each downward bellmouth is mud hole, is distributed with per a piece of biconial plate bottom surface
Coarse salient point, when oil-polluted water is by DTS coalescing-plate fillers, these coarse salient points can catch very small oil droplet,
Oil droplet is changed from small to big by 45 ° of upward taper surfaces, complete local oil droplet coalescence, so as to be easier under buoyancy to gather
The oil droplet of knot is floated on the water surface from upward bellmouth.Equally, 45 ° of DTS coalescing-plates filler are designed to inferior pyramidal slag-drip opening,
The greasy filth after coalescence and solid suspension is sunk because of gravity, coalesce in downward taper recess and fall into down by optic panel
The separator settling zone in portion, this design is very beneficial for the separation of greasy filth floccule and solid, it is therefore prevented that coalescing-plate filler
Blocking, the fluid higher to viscous crude and solids content have extraordinary adaptability.It has treatment effeciency height, the scope of application
Extensively, the features such as easy cleaning, easy care, installation operation are convenient, parallel-plate structure is arranged, separative efficiency is up to 99%.
In the present embodiment, the high-temperature oil gas refrigerated separation step of said apparatus is as follows：
1) high-temperature gas mixture A is by spraying cooling pipe 1, and multi-stage spray component 19 increases pressure-activated by pump operation,
5, after spraying cooling are typically first opened, into the bottom of scrubber condenser 2, according to pH meter show value, general pH meter is shown as 4~
5, answer the water pump 11 of scrubber condenser bottom operating always, now, measuring pump automatic start, the alkali lye of the inside of lye tank (vat) 10
Slowly squeeze into pipeline, it is automatic to close after measuring pump 13, acid-base neutralization until pH meter is shown as 7 or so, obtain certain impurity
Oil water mixture and rich gas B；
2) the oil water mixture pump 11 of scrubber condenser 2 is evacuated to automatic filter 3, automatic filter is that liquid is complete certainly
Dynamic scraper filter, liquid is flowed into from filter inlet, flowed from up to down, is flowed to and is exported through cartridge surface；When filter core table
When face is collected into a certain amount of mud, the scraper of motor driving assembling adjuster is close to cartridge surface rotation, strikes off mud, mud
Collecting chamber is gathered in descending liquid, when a certain amount of mud is arrived in accumulation, automatic blowdown valve opens collecting chamber, will contain high concentration miscellaneous
The mud discharge of matter, reenters the processing of reactor high temperature cabonization.Oil water mixture after filtering enters 4 points of oil water separator
From,
3) waste water that automatic filter 3 is discharged enters oil water separator 4, and the bio oil C of collection is evacuated to automatically as product
Oil storage tank, the waste water D after oil removing is largely recycled as spray liquid, and redundance drains into wastewater treatment facility processing automatically.
4) there is packing layer respectively by upper successively in the middle of scrubber condenser 2, there is demister on spray thrower, top, and rich gas B is obtained
To being sufficiently separated, cool down, further evolved, into surge tank 8, passed through by gas purifier 7 with roots blower 6 again after purification
The rich gas B of purification goes heating furnace gas burner heat supply；When rich gas buffer tank pressure is high, burner air gun is all opened
Open, close oil burning apparatus, by the rich gas heat supply that itself is produced, if unnecessary rich gas air gun has little time to burn, open it
His gas buffer tank does further buffering and stored；If also more gases are unnecessary, and pressure also (is typically set up to the upper limit
It is set to 60kpa), it can only be vented by liquid packing 9.
5) a part of waste water D after oil water separator separation passes through booster pump by water cooler 5 with cooling water system
12 work running water heat exchange cooling, then with water pump 11 squeeze into the multi-stage spray of spraying cooling pipe 1 spray and scrubber condenser 2 spray
Drench.
Preferable implementation example of the present utility model is the foregoing is only, the utility model is not limited to, it is all in this reality
Within new spirit and principle, any modification, equivalent substitution and improvements made etc. should be included in guarantor of the present utility model
Within the scope of shield.
Claims (6)
1. the high-temperature oil gas refrigerated separation device of a kind of organic solid castoff charcoal, it is characterised in that including connecting successively
Connect：
Spraying cooling pipe (1), the spraying cooling for high-temperature gas mixture；
Scrubber condenser (2), is further cooled down, acid-base neutralization and demisting to the high-temperature gas mixture being passed through, and obtains impure
Oil water mixture and rich gas (B)；
Automatic filter (3), for being filtered to described oil water mixture；
Oil water separator (4), for the oil water mixture after separating and filtering and obtains bio oil (C) and waste water (D).
2. high-temperature oil gas refrigerated separation device as claimed in claim 1, it is characterised in that：Described spraying cooling pipe (1) inclines
Tiltedly arrangement, and body is provided with 5~10 grades of spray assemblies (14).
3. high-temperature oil gas refrigerated separation device as claimed in claim 1, it is characterised in that：Described scrubber condenser (2) top
End is provided with demister (22) and sprayer unit (21), and centre is provided with packing layer (23), and the thickness of packing layer (23) is washing
The 1/2~1/5 of condenser (2) height.
4. high-temperature oil gas refrigerated separation device as claimed in claim 1, it is characterised in that：The top of the scrubber condenser (2)
Portion is connected with gas purifier (7) by pipeline, and for receiving at least one buffering of gas purifier (7) discharge gas
Tank (8).
5. high-temperature oil gas refrigerated separation device as claimed in claim 4, it is characterised in that：Described surge tank (8) is connected with
Liquid packing (9).
6. high-temperature oil gas refrigerated separation device as claimed in claim 1, it is characterised in that：Scrubber condenser (2) connection
There is acid-base neutralization circulation line, and the lye tank (vat) (10) and measuring pump (13) for accessing the circulation line are set.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201621490665.6U CN206385089U (en) | 2016-12-30 | 2016-12-30 | A kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal |
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| CN201621490665.6U CN206385089U (en) | 2016-12-30 | 2016-12-30 | A kind of high-temperature oil gas refrigerated separation device of organic solid castoff charcoal |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106590723A (en) * | 2016-12-30 | 2017-04-26 | 浙江天禄环境科技有限公司 | Cooling separation technology and device for high-temperature oil and gas generated during preparation of biological charcoal from organic solid waste |
-
2016
- 2016-12-30 CN CN201621490665.6U patent/CN206385089U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106590723A (en) * | 2016-12-30 | 2017-04-26 | 浙江天禄环境科技有限公司 | Cooling separation technology and device for high-temperature oil and gas generated during preparation of biological charcoal from organic solid waste |
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