CN107937008A - A kind of upgraded coal temperature reducing humidifier - Google Patents
A kind of upgraded coal temperature reducing humidifier Download PDFInfo
- Publication number
- CN107937008A CN107937008A CN201711351550.8A CN201711351550A CN107937008A CN 107937008 A CN107937008 A CN 107937008A CN 201711351550 A CN201711351550 A CN 201711351550A CN 107937008 A CN107937008 A CN 107937008A
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- CN
- China
- Prior art keywords
- humidifier
- upgraded coal
- coal
- scrubbing tower
- upgraded
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
Abstract
The present invention relates to a kind of upgraded coal temperature reducing humidifier, including revolution cooler, humidifier and scrubbing tower;The upgraded coal entrance of the upgraded coal discharge port connection humidifier top side of the revolution cooler, humidification motor spindle opposite side sets upgrading coal export, watering spray equipment is set at the top of humidifier, air intake is set close to humidifier one end of upgraded coal inlet side, offgas outlet is set at the top of the humidifier of upgrading coal export, offgas outlet connects scrubbing tower lower part tower reactor by pipeline, scrubbing tower top sets at least two-stage spray equipment, net gas outlet is set at the top of scrubbing tower, wash tower bottoms set washing water out, washing water out connects spray equipment by washing water circulating pipe, circulating pump and washings supplement entrance are set on washing water circulating pipe.The present invention makes the temperature of upgraded coal and moisture reach requirement, while the dust-laden steam to being produced in humidification cooling procedure is effectively treated, qualified discharge by cooling down the method being combined with humidification cooling indirectly.
Description
Technical field
The present invention relates to low-order coal upgrading technical field, more particularly to a kind of upgraded coal temperature reducing humidifier.
Background technology
For low-order coal after upright furnace is pyrolyzed upgrading, the temperature of product upgraded coal is about 600 DEG C, need to be cooled to 80 DEG C
It is processed again after left and right, transports storage;At present in country's low order pyrolytic process of coal, for cooling for upgraded coal
Processing has 2 kinds of common methods:One kind is that upgraded coal is cooled to 80 DEG C or so indirectly from 600 DEG C, and shortcoming is of high cost, Er Qieleng
But the dry material after usually has dust from flying, assembles the situation of spontaneous combustion, causes follow-up workshop section's dedusting pressure very big;Another work
Skill is directly soaked in pyrolysis furnace bottom, and upgraded coal is cooled to less than 80 DEG C, and shortcoming is that water consumption is big and generation is big
Steam is measured, undressed steam carries out a large amount of dust, can be escaped in follow-up workshop section, cause production environment severe.
The content of the invention
The present invention provides a kind of upgraded coal temperature reducing humidifier, by cooling down the side being combined with humidification cooling indirectly
Method, makes the temperature of upgraded coal and moisture reach requirement, while the dust-laden steam to being produced in humidification cooling procedure is effectively located
Reason, qualified discharge;On the one hand cooling load indirectly is reduced, weight of equipment, cost and operating cost are reduced, on the other hand to carrying
Matter coal is humidified, and is played dust suppression and is improved operating environment, reduces the effect of spontaneous combustion risk.
In order to achieve the above object, the present invention is realized using following technical scheme:
A kind of upgraded coal temperature reducing humidifier, including revolution cooler, humidifier and scrubbing tower;The revolution cooler is set
Water-cooling jacket, turns round the upgraded coal entrance of the upgraded coal discharge port connection humidifier top side of cooler, and humidification motor spindle is another
Side sets upgrading coal export, and spiral conveying mechanism is set between upgraded coal entrance and upgrading coal export;Watering spray is set at the top of humidifier
Shower device, sets air intake close to humidifier one end of upgraded coal inlet side, is set at the top of the humidifier of upgrading coal export
Offgas outlet, offgas outlet connect scrubbing tower lower part tower reactor by pipeline, and scrubbing tower top sets at least two-stage spray equipment, washs
Top of tower sets net gas outlet, and wash tower bottoms set washing water out, and washing water out is by washing water circulating pipe connection spray
Device, washs and circulating pump and washings supplement entrance is set on water circulating pipe.
Gas gathering mask is set above the humidifier internal screw conveyer structure, the top of gas gathering mask is connected with offgas outlet.
Net gas outlet at the top of the scrubbing tower connects diffuse channel, and air-introduced machine is set on diffuse channel.
The upgrading coal export of the humidifier sets temperature sensor and moisture detector, temperature sensor, moisture detector
Pass through control system and the water control valve interlocked control in watering spray equipment.
Compared with prior art, the beneficial effects of the invention are as follows:
1) using the method for sub-sectional cooling humidification;Upgraded coal is cooled to 200 DEG C by 600 DEG C by cooling down indirectly, so
It is cooled down twice and humidifies by humidifier again afterwards, upgraded coal temperature is down to 80 DEG C or so, moisture reaches 5% or so, full
The requirement of sufficient subsequent technique;
2) the dust-laden steam produced in humidification cooling procedure is effectively treated, accomplishes qualified discharge;So on the one hand
The load of indirect cooling device is reduced, reduces weight of equipment, cost and operating cost, is on the other hand realizing second of cooling
While upgraded coal is humidified, play dust suppression and improve operating environment, reduce upgraded coal storage when spontaneous combustion risk;
3) factory's recycle-water i.e. processed waste water is made full use of as spray water, realizes the purpose of clean manufacturing.
Brief description of the drawings
Fig. 1 is a kind of structure diagram of upgraded coal temperature reducing humidifier of the present invention.
In figure:1. turn round 2. humidifier of cooler, 3. scrubbing tower, the 4. watering spray equipment 6. of spiral conveying mechanism 5.
7. air-introduced machine of circulating pump
Embodiment
The embodiment of the present invention is described further below in conjunction with the accompanying drawings:
As shown in Figure 1, a kind of upgraded coal temperature reducing humidifier of the present invention, including revolution cooler 1,2 and of humidifier
Scrubbing tower 3;The revolution cooler 1 sets water-cooling jacket, 2 top one of upgraded coal discharge port connection humidifier of revolution cooler 1
The upgraded coal entrance of side, 2 bottom opposite side of humidifier set upgrading coal export, are set between upgraded coal entrance and upgrading coal export spiral
Conveying mechanism 4;The top of humidifier 2 sets watering spray equipment 5, and setting air close to 2 one end of humidifier of upgraded coal inlet side enters
Mouthful, offgas outlet is set close to the top of humidifier 2 of upgrading coal export, offgas outlet connects 3 lower part tower reactor of scrubbing tower by pipeline,
3 top of scrubbing tower sets at least two-stage spray equipment, and the top of scrubbing tower 3 sets net gas outlet, and 3 bottom of scrubbing tower sets washing water out,
Washing water out connects spray equipment by washing water circulating pipe, washs and circulating pump 6 and washings benefit are set on water circulating pipe
It is filled with mouth.
The top of the 2 internal screw conveyer structure 4 of humidifier sets gas gathering mask, and the top of gas gathering mask is connected with offgas outlet.
The net gas outlet at the top of scrubbing tower 3 connects diffuse channel, and air-introduced machine 7 is set on diffuse channel.
The upgrading coal export of the humidifier 2 sets temperature sensor and moisture detector, temperature sensor, moisture detector
Pass through control system and the water control valve interlocked control in watering spray equipment.
In the present invention, water-cooling jacket is set in the revolution cooler 1, for being carried out to about 600 DEG C of high temperature upgraded coals of temperature
Cooling indirectly, makes it be cooled to 200 DEG C or so.
Its interior setting watering spray equipment 5 of the humidifier 2, is cooled down and is humidified to about 200 DEG C of upgraded coal of temperature,
And the steam of generation is collected.
Set multi-stage spray device in the scrubbing tower 3, carry out condensation recycling to steam, and by the dust carried in steam into
Row washing, makes tail gas reach discharge standard, and tower bottoms is after of short duration sedimentation, and the water of bottom returns to humidifier 2, tower reactor top
Water returns to scrubbing tower 3 and carries out circulated sprinkling.
The air-introduced machine 7 is arranged on 3 downstream of scrubbing tower, is drawn for humidifier 2 to be included steam institute tail gas, by washing
Tail gas qualified discharge after the washing of tower 3, air-introduced machine 7 provide power for the gas flowing in whole system.
The outlet of humidifier 2 sets temperature sensor and moisture detector, for monitor the temperature of upgraded coal that will export and
Moisture, and stablize with 5 interlocked control of spray equipment of sprinkling water, automatic adjustment water spray, the temperature and water tariff collection for making upgraded coal.
Upgraded coal cooling heating technique based on a kind of upgraded coal temperature reducing humidifier of the present invention, including cooling indirectly
Process, humidification cooling procedure and vent gas treatment process;Specifically comprise the following steps:
1) enter revolution cooler 1 and cooling water indirect heat exchange from the upgraded coal of pyrolysis oven discharge, cooled down from more than 600 DEG C
To less than 200 DEG C, the upgraded coal after cooling that exchanges heat enters humidifier 2, by 4 downstream transport of spiral conveying mechanism, in humidifier 2
If sprinkling water spray equipment 5, upgraded coal is carried out plus water cools down and humidifies;
2) the upgraded coal inlet side of humidifier 2 sets air intake, the steam that will be produced by air as carrier after humidification
And dust is carried to scrubbing tower 3;Temperature is 75~85 DEG C after humidification cooling, and the upgraded coal that moisture is 4%~6% is from humidifier
2 afterbody discharge, is exported by ribbon conveyer;
3) top of scrubbing tower 3 sets spray equipment, and shower water sprays from up to down;Tail gas containing steam and dust is by washing
3 lower part of tower enter, directly contacted with tower bottoms in tower reactor first, recovered steam and major part dust, then with shower water
Reverse to contact, remaining a small amount of steam and dust enter tower bottoms after multistage is washed in tail gas;
4) purified gas is diffused under the effect of air-introduced machine 7 by the discharge of 3 tower top of scrubbing tower, and air-introduced machine 7 is at the same time to humidification
The extraction of 2 inner exhaust gas of machine provides power;Tower bottoms in scrubbing tower 3 is extracted out by circulating pump 6, and a part is sent to humidifier 2 and makees
For shower water, a part is sent to 3 top circulated sprinkling of scrubbing tower;The top of scrubbing tower 3 sets washings supplement entrance, supplement new water with
Sprayed after the mixing of circulated sprinkling water.
Temperature-detecting device and moisture detector are set in the upgraded coal exit of humidifier 2, after monitoring humidification cooling
Upgraded coal temperature and moisture, and by control system to sprinkle water spray equipment 5 water-spraying amount automatically adjust, make from
The temperature and water tariff collection for the upgraded coal that humidifier 2 is discharged are stablized.
The new water of supplement is the recycle-water from plant chimney stalk processing system.
Upgraded coal safe transport, storage can be realized using technique of the present invention, and achieve the purpose that clean manufacturing.
In Fig. 1, the instrument for indicating symbol T is temperature sensor, and the instrument for indicating symbol W is moisture detector, indicates symbol
The instrument of number F is flowmeter.
The foregoing is only a preferred embodiment of the present invention, but protection scope of the present invention be not limited thereto,
Any one skilled in the art the invention discloses technical scope in, technique according to the invention scheme and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (4)
1. a kind of upgraded coal temperature reducing humidifier, it is characterised in that including revolution cooler, humidifier and scrubbing tower;Described time
Turn cooler and set water-cooling jacket, turn round the upgraded coal entrance of the upgraded coal discharge port connection humidifier top side of cooler, add
Wet motor spindle opposite side sets upgrading coal export, and spiral conveying mechanism is set between upgraded coal entrance and upgrading coal export;Humidifier top
Portion sets watering spray equipment, and air intake is set close to humidifier one end of upgraded coal inlet side, close to adding for upgrading coal export
Offgas outlet is set at the top of wet machine, offgas outlet connects scrubbing tower lower part tower reactor by pipeline, and scrubbing tower top sets at least two-stage spray
Shower device, scrubbing tower top set net gas outlet, and wash tower bottoms set washing water out, and washing water out is by washing water-circulating pipe
Road connects spray equipment, washs and circulating pump and washings supplement entrance are set on water circulating pipe.
2. a kind of upgraded coal temperature reducing humidifier according to claim 1, it is characterised in that the humidifier inside spin is defeated
Send and gas gathering mask is set above mechanism, the top of gas gathering mask is connected with offgas outlet.
3. a kind of upgraded coal temperature reducing humidifier according to claim 1, it is characterised in that net at the top of the scrubbing tower
Gas outlet connects diffuse channel, and air-introduced machine is set on diffuse channel.
A kind of 4. upgraded coal temperature reducing humidifier according to claim 1, it is characterised in that the upgraded coal of the humidifier
Outlet sets temperature sensor and moisture detector, and temperature sensor, moisture detector pass through control system and watering spray equipment
In water control valve interlocked control.
Priority Applications (1)
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CN201711351550.8A CN107937008A (en) | 2017-12-15 | 2017-12-15 | A kind of upgraded coal temperature reducing humidifier |
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CN201711351550.8A CN107937008A (en) | 2017-12-15 | 2017-12-15 | A kind of upgraded coal temperature reducing humidifier |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110205150A (en) * | 2019-07-02 | 2019-09-06 | 北京康威盛热能技术有限责任公司 | A kind of improved coking coal humidifying method and apparatus |
CN112834049A (en) * | 2021-01-13 | 2021-05-25 | 中冶长天国际工程有限责任公司 | Method and system for secondary detection and secondary treatment of high-temperature activated carbon |
CN112857577A (en) * | 2021-01-08 | 2021-05-28 | 湖南中冶长天节能环保技术有限公司 | Method and system for detecting and secondarily treating high-temperature activated carbon |
CN112870913A (en) * | 2021-01-13 | 2021-06-01 | 中冶长天国际工程有限责任公司 | Method and system for extinguishing fire and reducing temperature of active carbon of front discharge hopper of adsorption tower |
CN112870601A (en) * | 2021-01-13 | 2021-06-01 | 中冶长天国际工程有限责任公司 | Method and system for secondary fire extinguishing and cooling treatment of high-temperature activated carbon |
Citations (2)
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CN102191065A (en) * | 2011-03-29 | 2011-09-21 | 山西星宇舟焦化工程设计有限公司 | Dry-wet combined coke quenching device |
CN207738702U (en) * | 2017-12-15 | 2018-08-17 | 中冶焦耐(大连)工程技术有限公司 | A kind of upgraded coal temperature reducing humidifier |
-
2017
- 2017-12-15 CN CN201711351550.8A patent/CN107937008A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102191065A (en) * | 2011-03-29 | 2011-09-21 | 山西星宇舟焦化工程设计有限公司 | Dry-wet combined coke quenching device |
CN207738702U (en) * | 2017-12-15 | 2018-08-17 | 中冶焦耐(大连)工程技术有限公司 | A kind of upgraded coal temperature reducing humidifier |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110205150A (en) * | 2019-07-02 | 2019-09-06 | 北京康威盛热能技术有限责任公司 | A kind of improved coking coal humidifying method and apparatus |
CN110205150B (en) * | 2019-07-02 | 2022-03-04 | 北京康威盛热能技术有限责任公司 | Improved coking coal moisture control method and equipment |
CN112857577A (en) * | 2021-01-08 | 2021-05-28 | 湖南中冶长天节能环保技术有限公司 | Method and system for detecting and secondarily treating high-temperature activated carbon |
CN112834049A (en) * | 2021-01-13 | 2021-05-25 | 中冶长天国际工程有限责任公司 | Method and system for secondary detection and secondary treatment of high-temperature activated carbon |
CN112870913A (en) * | 2021-01-13 | 2021-06-01 | 中冶长天国际工程有限责任公司 | Method and system for extinguishing fire and reducing temperature of active carbon of front discharge hopper of adsorption tower |
CN112870601A (en) * | 2021-01-13 | 2021-06-01 | 中冶长天国际工程有限责任公司 | Method and system for secondary fire extinguishing and cooling treatment of high-temperature activated carbon |
CN112870601B (en) * | 2021-01-13 | 2022-08-16 | 中冶长天国际工程有限责任公司 | Method and system for secondary fire extinguishing and cooling treatment of high-temperature activated carbon |
CN112870913B (en) * | 2021-01-13 | 2023-02-10 | 中冶长天国际工程有限责任公司 | Method and system for extinguishing fire and reducing temperature of active carbon of front discharge hopper of adsorption tower |
CN112834049B (en) * | 2021-01-13 | 2024-05-03 | 中冶长天国际工程有限责任公司 | Method and system for secondary detection and secondary treatment of high-temperature activated carbon |
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