CN206424702U - A kind of carbon black piece-rate system and its production system - Google Patents
A kind of carbon black piece-rate system and its production system Download PDFInfo
- Publication number
- CN206424702U CN206424702U CN201720104633.6U CN201720104633U CN206424702U CN 206424702 U CN206424702 U CN 206424702U CN 201720104633 U CN201720104633 U CN 201720104633U CN 206424702 U CN206424702 U CN 206424702U
- Authority
- CN
- China
- Prior art keywords
- carbon black
- tail gas
- exhaust gas
- water
- cooling
- Prior art date
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model provides a kind of carbon black piece-rate system and its production system, is related to the plain preparing technical field of charcoal.The carbon black piece-rate system includes the first tail gas pipeline, collection system, second tail gas pipeline and exhaust treatment system, collection system includes multiple bag hoses, the import of each bag hose with the first tail gas pipeline connection, and the top exit of each bag hose with the second tail gas pipeline connection, exhaust treatment system includes adsorption dewatering device and gas-liquid separating and dehydrating device, gas-liquid separation dehydration device is liquefied the vapor in tail gas by cooling device, separated the available gas in moisture and tail gas by steam-water separator again, the moisture in tail gas is set sufficiently to be removed.The carbon black production system includes above-mentioned carbon black tail gas processing system, and it can sufficiently be removed the moisture in carbon black tail gas, by active ingredient Returning reacting system, improve raw material availability.
Description
Technical field
The utility model is related to the plain preparing technical field of charcoal, in particular to a kind of carbon black piece-rate system and its production
System.
Background technology
Carbon black also known as carbon black, are a kind of amorphous carbon.Gently, pine and superfine black powder, surface area is very big, scope from
10—3000m2/ g, is that carbonaceous material (coal, natural gas, heavy oil, fuel oil etc.) fires under conditions of lack of air through incomplete
Burn or product obtained by being thermally decomposed.
Typically in the production technology of carbon black, by the way of natural gas Pintsch process, contain pair in generation carbon black tail gas
Product vapor, carbon dioxide and carbon monoxide etc., and tail gas has very high temperature.There is tail gas in carbon black process to take off
Water is insufficient, and separates halfway problem.
Utility model content
The purpose of this utility model is to provide a kind of carbon black piece-rate system, and it is by the tail gas after carbon black collection system
By the adsorption dewatering device and gas-liquid separating and dehydrating device set gradually, the moisture in tail gas is sufficiently separated, have
Effect component is recycled utilization, improves the production efficiency of carbon black.
Another object of the present utility model is to provide a kind of carbon black production system, and it can be by the moisture in carbon black tail gas
Sufficiently removed, active ingredient is reused, improve raw material availability.
What the utility model was realized in：
A kind of carbon black piece-rate system, it includes the first tail gas pipeline, collection system, the second tail gas pipeline, burgy delivery pipe
Road and exhaust treatment system, collection system include multiple bag hoses, the import of each bag hose with the first tail gas pipeline connection,
The outlet at bottom of each bag hose connect with burgy transfer pipeline, and each the top exit of bag hose with the second offgas duct
Road is connected, and exhaust treatment system includes adsorption dewatering device and gas-liquid separating and dehydrating device, and adsorption dewatering device includes interior load
The multiple adsorption dewatering towers for having adsorbent and being sequentially connected in series, the air inlet of adsorption dewatering tower and the second tail gas pipeline connection, absorption
The gas outlet of dehydrating tower is connected with the air inlet of gas-liquid separation dehydration device.
Further, in the utility model preferred embodiment, above-mentioned collection system also includes being used to store carbon black
Burgy storage tank, the import of burgy storage tank is connected with the one end of burgy transfer pipeline away from bag hose.
Further, in the utility model preferred embodiment, the charcoal for purging is provided with above-mentioned bag hose
The back blowing machine of black powder.
Further, in the utility model preferred embodiment, above-mentioned gas-liquid separation dehydration device includes cooling device
And steam-water separator, the air inlet of cooling device connects with the gas outlet of adsorption dewatering tower, the gas outlet of cooling device and carbonated drink
The water inlet and delivery port of Cooling Water turnover are provided with the inlet communication of separator, cooling device.
Further, in the utility model preferred embodiment, above-mentioned cooling device includes spray column and tail gas is cooled down
Device, the air inlet of spray column is connected with the gas outlet of adsorption dewatering device, the gas outlet of spray column and the air inlet of exhaust gas cooler
Mouth connection, the gas outlet of exhaust gas cooler and the inlet communication of steam-water separator.
Further, in the utility model preferred embodiment, above-mentioned cooling device also includes the bottom of towe with spray column
The first cooling water storage tank that delivery port is connected with the bottom delivery port of exhaust gas cooler, the water inlet of spray column and the first cooling
Water storage tank is connected by first circulation water pipe.
Further, in the utility model preferred embodiment, above-mentioned spray column is provided with multiple water inlets from top to bottom
Mouthful, each water inlet is connected with the first cooling water storage tank.
Further, in the utility model preferred embodiment, above-mentioned exhaust gas cooler includes the one-level set gradually
Exhaust gas cooler and two grades of exhaust gas coolers, one-level exhaust gas cooler and two grades of exhaust gas coolers are respectively provided with bottom delivery port, cold
But the bottom delivery port of water inlet and coolant outlet, one-level exhaust gas cooler and two grades of exhaust gas coolers with the first cooling water
Storage tank is connected, and cooling device also includes the second cooling water storage tank, freezing unit and the freezing water pot for storing chilled water, second
The delivery port of cooling water storage tank is connected by second circulation water pipe with the cooling water inlet of one-level exhaust gas cooler, freezing water pot with
Unit connection is freezed, and the delivery port of freezing water pot is connected by the cooling water inlet of the 3rd circulating water pipe and two grades of exhaust gas coolers
It is logical.
Further, in the utility model preferred embodiment, the cooling water inlet of above-mentioned one-level exhaust gas cooler with
The water inlet of freezing water pot is connected with circulating water main.
A kind of carbon black production system, including above-mentioned carbon black piece-rate system and reaction system, reaction system and the first offgas duct
Road is connected.
The beneficial effects of the utility model are：The carbon black piece-rate system that the utility model is obtained by above-mentioned design, by tail
Gas is collected carbon black by the bag hose in collection system, and gas is passed through into the adsorption dewatering device in exhaust treatment system again
With the processing of gas-liquid separating and dehydrating device, make the effect of dehydration more preferable.Gas-liquid separation dehydration device will by cooling device
Vapor liquefaction in tail gas, then separated the available gas in moisture and tail gas by steam-water separator, make in tail gas
Moisture sufficiently removed, and the active principle in tail gas is recycled utilization, improve the production efficiency of carbon black.
The carbon black production system that the utility model is provided includes above-mentioned carbon black piece-rate system, and it can obtain the moisture in carbon black tail gas
Sufficiently removing, active ingredient is recycled, raw material availability is improved.
Brief description of the drawings
, below will be to required in embodiment in order to illustrate more clearly of the technical scheme of the utility model embodiment
The accompanying drawing used is briefly described, it will be appreciated that the following drawings illustrate only some embodiments of the present utility model, therefore not
The restriction to scope is should be considered as, for those of ordinary skill in the art, on the premise of not paying creative work,
Other related accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation for the carbon black piece-rate system that the utility model embodiment is provided；
Fig. 2 is the structural representation of collection system in Fig. 1；
Fig. 3 is the structural representation for the adsorption dewatering device that the utility model embodiment is provided；
Fig. 4 is the structural representation for the gas-liquid separation dehydration device that the utility model embodiment is provided；
Fig. 5 is the structural representation of spray column in Fig. 4；
Fig. 6 is the structural representation of steam-water separator in Fig. 4.
Icon：100- carbon black piece-rate systems；110- collection systems；120- adsorption dewatering devices；130- gas-liquid separations are dehydrated
Device；140- exhaust treatment systems；112- imports；114- is exported；142- air inlets；W1- bottom of towe delivery ports；The water outlet of W2- bottoms
Mouthful；W3- bottoms delivery port；W4- bottoms delivery port；W5- water inlets；W6- cooling water inlets；W7- coolant outlets；W8- is cooled down
Water inlet；W9- coolant outlets；W10- water inlets；A0- air inlets；A1- gas outlets；A2- air inlets；A3- gas outlets；A4- enters
Gas port；A5- gas outlets；A6- air inlets；A7- gas outlets；A8- imports；A9- is exported；G1- first circulation water pipes；G2- second is followed
Ring water pipe；The circulating water pipes of G3- the 3rd；G4- circulation lines；G5- connecting pipelines；V1- the first cooling water storage tanks；V2- second is cooled down
Water storage tank；V3- freezes water pot；L1- freezes unit；T1- adsorption dewatering towers；T2- spray columns；C1- one-level exhaust gas coolers；C2-
Two grades of exhaust gas coolers；F1- steam-water separators；132- packing layers；134- spray pipelines；136- mouth sprays；The tail gas of 180- first
Pipeline；150- the second tail gas pipelines；160- bag hoses；162- outlet at bottoms；164- imports；166- top exits；170- burgy
Storage tank；172- imports；190- burgy transfer pipelines.
Embodiment
To make the purpose, technical scheme and advantage of the utility model embodiment clearer, below in conjunction with this practicality
Accompanying drawing in new embodiment, the technical scheme in the utility model embodiment is clearly and completely described, and shows
So, described embodiment is a part of embodiment of the utility model, rather than whole embodiments.Based on this practicality
Embodiment in new, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of the utility model protection.Therefore, implementation of the present utility model below to providing in the accompanying drawings
The detailed description of mode is not intended to limit claimed scope of the present utility model, but is merely representative of of the present utility model
Selected embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not making creative labor
The every other embodiment obtained under the premise of dynamic, belongs to the scope of the utility model protection.
In description of the present utility model, it is to be understood that term " on ", " under ", "front", "rear", " top ", " bottom ",
The orientation or position relationship of the instructions such as " interior ", " outer " are, based on orientation shown in the drawings or position relationship, to be for only for ease of and retouch
State the utility model and simplify and describe, rather than indicate or imply signified equipment or element must have specific orientation, with
Specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.
In addition, term " first ", " second " are only used for describing purpose, and it is not intended that indicating or implying relative importance
Or the implicit quantity for indicating indicated technical characteristic.Thus, define " first ", the feature of " second " can express or
Implicitly include one or more this feature.In description of the present utility model, " multiple " are meant that two or two
More than, unless otherwise specifically defined.
In the utility model, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " Gu
It is fixed " etc. term should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integrally；Can be
Mechanically connect or electrically connect；Can be joined directly together, can also be indirectly connected to by intermediary, can be two
The connection of element internal or the interaction relationship of two elements.For the ordinary skill in the art, can basis
Concrete condition understands concrete meaning of the above-mentioned term in the utility model.
Embodiment
Fig. 1 is refer to, the present embodiment provides a kind of carbon black piece-rate system 100, it includes the first tail gas pipeline 180, collection
System 110, the second tail gas pipeline 150 and exhaust treatment system 140, the first tail gas pipeline 180 and the import of collection system 110
112 are connected, and the second tail gas pipeline 150 is connected with the outlet 114 of collection system 110, and the second tail gas pipeline 150 and vent gas treatment
The air inlet 142 of system 140 is connected.
Specifically, Fig. 2 is refer to, collection system 110 includes burgy transfer pipeline 190 and multiple bag hoses 160, each bag
The import 164 of filter 160 is connected with the first tail gas pipeline 180, and the outlet at bottom 162 of each bag hose 160 is defeated with burgy
Pipeline 190 is sent to connect, and the top exit 166 of each bag hose 160 is connected with the second tail gas pipeline 150.Tail gas is by first
Tail gas pipeline 180 enters collection system 110, separates the carbon black in tail gas by multiple bag hoses 160, after treatment
Tail gas enter follow-up exhaust treatment system 140.It should be noted that the structure and principle of bag hose 160 and general bag hose
All same, is that dusty gas is passed through into bag-shaped filter cloth, removes grit therein.
Further, collection system 110 also includes the burgy storage tank 170 for being used to store carbon black, the import of burgy storage tank 170
172 connect with the one end of burgy transfer pipeline 190 away from bag hose 160.The carbon black products that collection system 110 is isolated are carried out
Collect, facilitate follow-up processing.The back blowing machine (not shown) of the hydrocarbon black powder for purging is provided with bag hose 160,
The carbon black pellet in bag hose 160 is periodically set to enter burgy storage tank 170 by burgy transfer pipeline 190 using back blowing machine, together
When avoid carbon black and block bag hose 160 and burgy transfer pipeline 190, improve the service life of bag hose 160.Need explanation
, the carbon black after collection system 110 in tail gas separated, and vapor, carbon monoxide and two are mainly contained in tail gas
Carbonoxide etc..
Incorporated by reference to Fig. 2 and Fig. 3, exhaust treatment system 140 includes adsorption dewatering device 120 and gas-liquid separating and dehydrating device
130, adsorption dewatering device 120 includes the interior multiple adsorption dewatering tower T1 for being filled with adsorbent and being sequentially connected in series, adsorption dewatering tower
T1 air inlet A0 is connected with the second tail gas pipeline 150, adsorption dewatering tower T1 gas outlet A1 and gas-liquid separation dehydration device 130
Air inlet A2 connection.Tail gas Jing Guo collection system 110 is first passed around to the adsorption dewatering tower T1 on adsorption dewatering device 120
Moisture is separated into gas-liquid separation dehydration device 130 after being absorbed to vapor, is easy to recycle available gas
Carbon monoxide and carbon dioxide.
Further, gas-liquid separation dehydration device 130 includes cooling device and steam-water separator F1, adsorption dewatering tower T1's
Gas outlet A1 is connected with the air inlet A2 of cooling device, and the gas outlet A7 and steam-water separator F1 of cooling device import A8 connect
It is logical, the water inlet and delivery port of Cooling Water turnover are provided with cooling device.Specifically, cooling device uses recirculated cooling water
As cooling medium, tail gas is first passed around after cooling device cooling, vapor is liquefied, is entered back into steam-water separator F1 and isolate
Aqueous water, active principle carbon monoxide and carbon dioxide, which are returned, to be recycled.
It should be noted that using carbolineum to produce carbon black for raw material, the carbon black tail gas by collection system 110 is mainly contained
Vapor, carbon monoxide and carbon dioxide etc. are, it is necessary to vapor be removed, then active principle carbon monoxide and carbon dioxide are entered
Row is recycled.Carbon black tail gas processing system 140 by tail gas by, by multiple adsorption dewatering tower T1, making the vapor in tail gas
Obtain initial absorption in adsorption tower, then vapor is liquefied after being cooled by cooling device, finally by steam-water separation
Device F1 is again separate out moisture, active principle carbon monoxide and carbon dioxide is recycled utilization, improves the utilization of raw material
Rate, and the carbon black productivity that whole production of carbon black is set.
Preferably, each adsorption dewatering tower T1 adsorption stuffing is has molecular sieve, and molecular sieve can have as adsorption stuffing
Vapor in the absorption tail gas of effect, after multiple adsorption dewatering tower T1 adsorbing separation, the content of the vapor in tail gas
Significantly reduce, be conducive to improving removal efficiency of the follow-up gas-liquid separation dehydration device 130 to moisture.
It should be noted that in other embodiments, adsorption dewatering tower T1 adsorption stuffing can be other kinds, such as
Activated carbon, aluminum oxide or Kiselgel A etc..Different fillers can also be filled with respectively in adsorption dewatering tower T1 tower tops and bottom of towe.
Further, cooling device includes spray column T2 and exhaust gas cooler, and spray column T2 air inlet A2 and absorption are de-
The gas outlet A1 connections of water installations 120, spray column T2 gas outlet A3 is connected with the air inlet A4 of exhaust gas cooler, tail gas cooling
The gas outlet A7 and steam-water separator F1 of device import A8 are connected.Spray column T2 plays preliminary cooling effect to tail gas, then passes through
Cross exhaust gas cooler tail gas further cools, the vapor in tail gas is liquefied, improve the removal efficiency of moisture, so as to improve
The separative efficiency of exhaust gas processing device, makes the active principle in separated tail gas purer.
Further, above-mentioned cooling device also includes the bottom of towe delivery port W1 with spray column T2 and the bottom of exhaust gas cooler
The water inlet W5 and the first cooling water storage tank V1 for the first cooling water storage tank V1, spray column T2 that delivery port W2 is connected pass through first
Circulating water pipe G1 is connected.Because the temperature of the tail gas of carbon black is very high, the cooling used during preliminary to the tail gas coolings of spray column T2 is situated between
Matter temperature is unsuitable too low, has been raised by spray column T2 and the recirculated water of exhaust gas cooler temperature, by this part recirculated water
It is stored in the first cooling water storage tank V1 and is easy to carry out tail gas preliminary cooling as spray column T2 cooling medium.
Further, above-mentioned spray column T2 is provided with multiple water inlet W5 from top to bottom, and each water inlet W5 is with first
Cooling water storage tank V1 is connected.Multiple water inlet W5 setting improves spray column T2 operating efficiency, and tail gas is passed through into multiple sprays
The cooling of mouth 136 is drenched, entering back into cooling device makes vapor sufficiently be liquefied.
Specifically, Fig. 4 is refer to, spray column T2 each water inlet W5 cooling medium is all from same pipeline, correspondence
Each water inlet W5 sets and is provided with multiple mouth sprays 136 on a spray pipeline 134, each spray pipeline 134, in spray
The lower section on shower pipe road 134 is provided with packing layer 132, and tail gas and cooling water are fully contacted in packing layer 132, improve heat transfer effect
Rate, making the temperature of tail gas significantly reduces, into follow-up exhaust gas cooler.
Specifically, it is made up of the tail gas after being cooled down after apparatus for supercooling aqueous water, carbon monoxide and carbon dioxide,
Need to remove aqueous water, by active principle carbon monoxide and carbon dioxide recovery.Fig. 5 is refer to, steam-water separator F1 is utilized
The effect of blower fan, makes gas spiral formula move upwards, due to the effect of aqueous water gravity, and deposition is got off, and gas is from steam-water separation
Device F1 outlet A9 outputs, and aqueous water enters the first cooling water storage tank V1 from steam-water separator F1 bottom delivery port W4.Vapour
Separator F1 import and export direction, can be by the flow direction of air-blower control gas it can also be provided that top is exported into lower section
It can be separated gas and aqueous water, specific operation principle is identical with the operation principle of existing steam-water separator.
Further, referring once again to Fig. 3, exhaust gas cooler includes the one-level exhaust gas cooler C1 set gradually and two grades
Exhaust gas cooler C2, one-level exhaust gas cooler C1 have bottom delivery port W2, cooling water inlet W6 and coolant outlet W7, two grades
Exhaust gas cooler C2 has bottom delivery port W3, cooling water inlet W8 and coolant outlet W9.Specifically, one-level exhaust gas cooler
C1 and two grade of exhaust gas cooler C2 bottom delivery port W3 is connected with the first cooling water storage tank V1, and cooling device also includes second
Cooling water storage tank V2, the freezing unit L1 and freezing water pot V3 for storing chilled water, the second cooling water storage tank V2 delivery port
Connected by second circulation water pipe G2 with one-level exhaust gas cooler C1 cooling water inlet W6, freezing water pot V3 and freezing unit L1
Connected by circulation line G4, and freezing water pot V3 delivery port passes through the 3rd circulating water pipe G3's and two grades of exhaust gas cooler C2
Cooling water inlet W8 is connected.
It should be noted that exhaust gas cooler is set to one-level exhaust gas cooler C1 and two grades of exhaust gas cooler C2, and
The temperature of one-level exhaust gas cooler C1 and two grades of exhaust gas cooler C2 cooling medium is different, one-level exhaust gas cooler C1 cooling
Medium is from general recirculated cooling water, and two grades of exhaust gas cooler C2 cooling medium is from by the L1 coolings of freezing unit
Chilled water, will sufficiently liquefy after the vapor in tail gas after cooling down twice, enters back into follow-up steam-water separator F1, improve
The separative efficiency of vapour-liquid.In addition, freezing unit L1 is mainly made up of refrigeration compressor, operation principle and existing freezing unit L1
It is identical, recirculated cooling water is cooled by refrigeration compressor using refrigerant vapor.
Further, above-mentioned two grades of exhaust gas cooler C2 coolant outlet W9 and freezing water pot V3 water inlet W10 connect
It is logical.One-level exhaust gas cooler C1 cooling water inlet W6 and freezing water pot V3 water inlet W10 is by connecting pipeline G5 with following
Ring supply mains connects.One-level exhaust gas cooler C1 coolant outlet W7 is connected with circulating water main, or will be from one-level tail gas
The cooling water of cooler C1 coolant outlet W7 outputs is discharged.It is such to be circularly set the utilization for improving cooling water
Rate, has reached water-saving purpose, production cost is reduced to a certain extent.
It should be noted that circulating water main is connected with big water storage system, by the recirculated cooling water in the water storage system
Introduce carbon black tail gas processing system 140 and be used as cooling medium.Other first circulation water pipe G1, second circulation water pipe G2, the 3rd follow
Water circulating pump is provided with the circulation lines such as ring water pipe G3, can be the recirculated water pump group of parallel connection or following for series connection
Ring water pump group, the power according to needed for affiliated pipeline is configured.
The present embodiment also provides a kind of carbon black production system, including above-mentioned carbon black piece-rate system 100.At carbon black tail gas
Carbon monoxide and carbon dioxide are mainly contained in the tail gas that reason system 140 is separated, this portion gas is subjected to recycling, had
Effect improves the utilization rate of raw material and the conversion ratio of carbon black, and production cost is reduced to a certain extent.
In summary, the utility model provides a kind of carbon black piece-rate system 100, and it is by collection system 110 by tail gas
In carbon black pellet be collected, and the vapor in tail gas is existed by multiple adsorption dewatering tower T1 in the tail gas after processing
Obtain initial absorption in adsorption tower, then vapor is liquefied after being cooled by cooling device, finally by steam-water separator
F1 is again separate out moisture, active principle carbon monoxide and carbon dioxide is recycled utilization, improves the utilization rate of raw material,
The carbon black productivity set with whole production of carbon black；Cooling water in spray column T2 and cooling device is collected in the storage of the first cooling water
It is easy to the cooling preliminary to tail gas progress in groove V1 as spray column T2 cooling medium, realizes the mesh that multi-section cools
's；Exhaust gas cooler is set to one-level exhaust gas cooler C1 and two grades of exhaust gas cooler C2, and one-level exhaust gas cooler C1 and
The temperature of two grades of exhaust gas cooler C2 cooling medium is different, will sufficiently be liquefied after the vapor in tail gas after cooling down twice,
Follow-up steam-water separator F1 is entered back into, the separative efficiency of vapour-liquid is improved.The utility model additionally provides a kind of production of carbon black
System, it includes above-mentioned carbon black piece-rate system 100, and one is mainly contained in the tail gas separated by carbon black tail gas processing system 140
Carbonoxide and carbon dioxide, recycling is carried out by this portion gas, effectively increases the utilization rate of raw material and turning for carbon black
Rate.
Preferred embodiment of the present utility model is the foregoing is only, the utility model is not limited to, for
For those skilled in the art, the utility model can have various modifications and variations.It is all in spirit of the present utility model and former
Within then, any modification, equivalent substitution and improvements made etc. should be included within protection domain of the present utility model.
Claims (10)
1. a kind of carbon black piece-rate system, it is characterised in that it includes the first tail gas pipeline, collection system, the second tail gas pipeline, powder
Charcoal transfer pipeline and exhaust treatment system, the collection system include multiple bag hoses, the import of each bag hose with
The first tail gas pipeline connection, the outlet at bottom of each bag hose is connected with the burgy transfer pipeline, and each
The top exit of the bag hose with the second tail gas pipeline connection；
The exhaust treatment system includes adsorption dewatering device and gas-liquid separating and dehydrating device, and the adsorption dewatering device includes interior
The multiple adsorption dewatering towers for being filled with adsorbent and being sequentially connected in series, the air inlet of the adsorption dewatering tower and second offgas duct
Road is connected, and the gas outlet of the adsorption dewatering tower is connected with the air inlet of the gas-liquid separation dehydration device.
2. carbon black piece-rate system according to claim 1, it is characterised in that the collection system also includes being used to store carbon black
Burgy storage tank, the import of the burgy storage tank connects with the described one end of burgy transfer pipeline away from the bag hose.
3. carbon black piece-rate system according to claim 2, it is characterised in that be provided with each bag hose for blowing
The back blowing machine for the hydrocarbon black powder swept.
4. carbon black piece-rate system according to claim 1, it is characterised in that the gas-liquid separation dehydration device includes cooling and filled
Put and steam-water separator, the air inlet of the cooling device is connected with the gas outlet of the adsorption dewatering tower, the cooling device
Gas outlet and the steam-water separator inlet communication, be provided with the cooling device Cooling Water turnover water inlet and
Delivery port.
5. carbon black piece-rate system according to claim 4, it is characterised in that the cooling device includes spray column and tail gas is cold
But device, the air inlet of the spray column is connected with the gas outlet of the adsorption dewatering device, the gas outlet of the spray column and institute
State the air inlet connection of exhaust gas cooler, the gas outlet of the exhaust gas cooler and the inlet communication of the steam-water separator.
6. carbon black piece-rate system according to claim 5, it is characterised in that the cooling device also includes and the spray column
Bottom of towe delivery port the first cooling water storage tank for being connected with the bottom delivery port of the exhaust gas cooler, the spray column enters
The mouth of a river is connected with the first cooling water storage tank by first circulation water pipe.
7. carbon black piece-rate system according to claim 6, it is characterised in that the spray column be provided with from top to bottom it is multiple enter
The mouth of a river, each water inlet is connected with the first cooling water storage tank.
8. carbon black piece-rate system according to claim 6, it is characterised in that the exhaust gas cooler includes one set gradually
Level exhaust gas cooler and two grades of exhaust gas coolers, the one-level exhaust gas cooler and two grades of exhaust gas coolers are respectively provided with bottom
The bottom of delivery port, cooling water inlet and coolant outlet, the one-level exhaust gas cooler and two grades of exhaust gas coolers goes out
The mouth of a river is connected with the first cooling water storage tank, and the cooling device also includes the second cooling water storage tank, freezing unit and for depositing
The freezing water pot of chilled water is stored up, the delivery port of the second cooling water storage tank is cold by second circulation water pipe and the one-level tail gas
But the cooling water inlet connection of device, the freezing water pot is connected with the freezing unit, and the delivery port of the freezing water pot leads to
The cooling water inlet that the 3rd circulating water pipe is crossed with two grades of exhaust gas coolers is connected.
9. carbon black piece-rate system according to claim 8, it is characterised in that the cooling water inlet of the one-level exhaust gas cooler
Connected with the water inlet of the freezing water pot with circulating water main.
10. a kind of carbon black production system, it is characterised in that including the carbon black piece-rate system any one of claim 1-9.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104633.6U CN206424702U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black piece-rate system and its production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104633.6U CN206424702U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black piece-rate system and its production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206424702U true CN206424702U (en) | 2017-08-22 |
Family
ID=59591820
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720104633.6U Expired - Fee Related CN206424702U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black piece-rate system and its production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206424702U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114644840A (en) * | 2022-04-25 | 2022-06-21 | 丰城黑豹炭黑有限公司 | Method and device for manufacturing carbon black pigment |
-
2017
- 2017-01-23 CN CN201720104633.6U patent/CN206424702U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114644840A (en) * | 2022-04-25 | 2022-06-21 | 丰城黑豹炭黑有限公司 | Method and device for manufacturing carbon black pigment |
| CN114644840B (en) * | 2022-04-25 | 2023-03-10 | 丰城黑豹炭黑有限公司 | Method and device for manufacturing carbon black pigment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101104825B (en) | Method for producing liquefied natural gas of mine gas | |
| CN203017963U (en) | Refrigeration-type compressed air cleaning dryer | |
| CN101703841B (en) | Device for collecting and recovering oil gas by condensation and absorption | |
| CN206424702U (en) | A kind of carbon black piece-rate system and its production system | |
| CN102296979B (en) | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source | |
| CN104019627A (en) | Moving small-size skid-mounted LNG liquefying device | |
| CN101857812B (en) | Medium-pressure shallow cooling purification system for oilfield associated gas | |
| CN206244740U (en) | Pipe natural gas heavy hydrocarbon removal unit | |
| CN206424759U (en) | A kind of carbon black tail gas processing system and carbon black production system | |
| CN206457444U (en) | A kind of carbon black production equipment and its production system | |
| CN105865145B (en) | A kind of coal gas gasification technique | |
| CN201722353U (en) | Medium-pressure shallow-condensing purification system for oilfield associated gas | |
| CN206300409U (en) | A kind of utilization associated gas isolates the processing unit of LPG and stable light hydrocarbon | |
| CN206508763U (en) | A kind of absorbent is without backflow regenerative system and absorption system | |
| CN208042615U (en) | A kind of coal chemical industry synthesis gas cryogenic separation co-production of methane gas system | |
| CN105964113B (en) | A kind of zero gas consumption compressed air drier by afterheat regeneration | |
| CN108079736B (en) | Flash evaporation gas purification and recovery system | |
| CN209098595U (en) | A kind of associated gas condensate recovery device for offshore marginal oilfield | |
| CN204987651U (en) | Explosion -proof liquefying plant of making an uproar falls in sleeve pipe gas | |
| CN209481601U (en) | A kind of heavy hydrocarbon separator and light ends unit for natural gas | |
| CN209706436U (en) | A kind of movable type skid scattered gas recycling device | |
| CN208717191U (en) | A kind of cryogenic separation system of low carbon olefin gas | |
| CN207527285U (en) | CNG gas stations utilize LNG cold energy dehydrating process systems | |
| CN208234866U (en) | A kind of liquefied natural gas purification device | |
| CN207493455U (en) | A kind of vehicular glycol dehydration device and absorption system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170822 Termination date: 20220123 |