CN209481574U - The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene - Google Patents
The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene Download PDFInfo
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- CN209481574U CN209481574U CN201822099049.3U CN201822099049U CN209481574U CN 209481574 U CN209481574 U CN 209481574U CN 201822099049 U CN201822099049 U CN 201822099049U CN 209481574 U CN209481574 U CN 209481574U
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- China
- Prior art keywords
- connect
- scrapper
- acetylene
- conveyors
- cooler
- 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.)
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- 239000002002 slurry Substances 0.000 title claims abstract description 44
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 title claims abstract description 38
- 239000002893 slag Substances 0.000 title claims abstract description 13
- RDYCRJVONVRAJS-UHFFFAOYSA-N [C].[Fe].[Sn] Chemical compound [C].[Fe].[Sn] RDYCRJVONVRAJS-UHFFFAOYSA-N 0.000 title claims abstract description 12
- 239000000843 powder Substances 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 150000001247 metal acetylides Chemical class 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 239000005997 Calcium carbide Substances 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
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- Carbon And Carbon Compounds (AREA)
Abstract
The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene, and the utility model relates to carbides to manufacture PVC technical field；The No.1 scrapper conveyor is set to the bottom of acetylene generator, No.1 scrapper conveyor is connect with No. two scrapper conveyors, No. two scrapper conveyors are set to the left lower of No.1 scrapper conveyor, slurry storage tank is connect with the right end of No.1 scrapper conveyor, No. two scrapper conveyors are connect with elevator, the upper end of elevator is connect with No. three scrapper conveyors, the right end of the slurry storage tank is connect with Pulp pump, the gas outlet of slurry storage tank is connect with cooler, Pulp pump is connect with reaction kettle, the connection of the lower end of reaction kettle and cooler, the upper end of cooler is connect with water ring compressor, water ring compressor is connect with acetylene surge tank, slurry is separated and reprocessed by scrapper conveyor, realize the production again and utilization of slurry.
Description
Technical field
The utility model relates to and carbide manufacture PVC technical field, and in particular to acetylene occur carbide slag slurries in extract
The separator of acetylene gas and tin iron carbon powder.
Background technique
The PVC acetylene of carbide manufacture at present occurs in technique, and the slurry generated after calcium carbide reaction is discharged to slag by overflow
It starches in dashpot, but part acetylene gas can be dissolved in slurry, acetylene gas is emptied from the top of slurry surge tank directly, was both caused
The wasting of resources generates insecurity factor and environmental pollution again, influences the normal operation of acetylene generating system, therefore can be to slurry
Acetylene and tin iron carbon powder in liquid are separated and recovered.
Utility model content
The purpose of this utility model is that in view of the drawbacks of the prior art and insufficient, provide that a kind of structure is simple, and design is closed
The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for reason, acetylene easy to use, passes through scraper plate to slurry
Machine is separated and is reprocessed, and realizes the production again and utilization of slurry.
In order to achieve the above purposes, the technical solution adopted by the utility model is: it include No.1 scrapper conveyor, slurry storage tank,
No. two scrapper conveyors, elevator, No. three scrapper conveyors, Pulp pump, reaction kettle, cooler, water ring compressor, acetylene surge tank；It is described
No.1 scrapper conveyor be set to the bottom of acetylene generator, No.1 scrapper conveyor connect with No. two scrapper conveyors, and No. two scrapper conveyors are set on one
The left lower of number scrapper conveyor, slurry storage tank are connect with the right end of No.1 scrapper conveyor, and No. two scrapper conveyors are connect with elevator, are promoted
The upper end of machine is connect with No. three scrapper conveyors, and the right end of the slurry storage tank is connect with Pulp pump, the gas outlet of slurry storage tank with
Cooler connection, Pulp pump are connect with reaction kettle, and the lower end connection of reaction kettle and cooler, the upper end of cooler and water ring compress
Machine connection, water ring compressor are connect with acetylene surge tank.
After adopting the above structure, the utility model has the beneficial effect that carbide slag slurries occur for acetylene described in the utility model
The middle separator for extracting acetylene gas and tin iron carbon powder, is separated and is reprocessed by scrapper conveyor to slurry, realize slurry
The advantages that production and utilization, the utility model have structure simple again, and setting is reasonable, low manufacture cost.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the flow process figure of the utility model.
Description of symbols:
No.1 scrapper conveyor 1, slurry storage tank 1-1, No. two scrapper conveyors 2,3, No. three scrapper conveyors 4 of elevator, Pulp pump 5, reaction
Kettle 6, cooler 7, water ring compressor 8, acetylene surge tank 9.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings.
Referring to as shown in Figure 1, present embodiment the technical solution adopted is that: it include No.1 scrapper conveyor 1, slurry store up
Tank 1-1, No. two scrapper conveyors 2, elevator 3, No. three scrapper conveyors 4, Pulp pump 5, reaction kettle 6, cooler 7, water ring compressors 8, second
Alkynes surge tank 9；The No.1 scrapper conveyor 1 is set to the bottom of acetylene generator, and the feed inlet and acetylene of No.1 scrapper conveyor 1 occur
The slurry mouth of device connects, and No.1 scrapper conveyor 1 is connect with No. two scrapper conveyors 2, and No. two scrapper conveyors 2 are set to the left side of No.1 scrapper conveyor 1
The feed inlet of lower part, No. two scrapper conveyors 2 is connect with the discharge port of No.1 scrapper conveyor 1, slurry storage tank 1-1 and No.1 scrapper conveyor 1
Right end connection, the outlet of No.1 scrapper conveyor 1 are connect with slurry storage tank 1-1, discharge port and the elevator 3 of No. two scrapper conveyors 2
Feed inlet connection, the discharge port of elevator 3 are connect with the feed inlet of No. three scrapper conveyors 4, the discharge nozzle of the slurry storage tank 1-1
It being connect with Pulp pump 5, the gas outlet of slurry storage tank 1-1 is connect with cooler 7, and Pulp pump 5 is connect with the feed inlet of reaction kettle 6,
The escape pipe of reaction kettle 6 is connect with the air inlet of cooler 7, and the gas outlet of cooler 7 and the air inlet of water ring compressor 8 connect
It connects, the gas outlet of water ring compressor 8 is connect with the air inlet of acetylene surge tank 9.
Tin iron carbon powder is transported to No. two scrapper conveyors 2 by No.1 scrapper conveyor 1 by the carbide slag slurries being discharged from generator bottom,
Carbide slag slurries flow in slurry storage tank 1-1, and No.1 scrapper conveyor 1 conveys the tin iron carbon powder to come and is transported to by No. two scrapper conveyors 2
In elevator 3, the tin iron carbon powder that No. two scrapper conveyors 2 are sent is passed through into the elevator 3 with spray and is transported to No. three scrapper conveyors 4,
The clean tin iron carbon powder that elevator 3 is sent is transported to outside battery limit (BL) by No. three scrapper conveyors 4 and is pulled away；Slurry storage tank 1-1 storage
There are the carbide slag slurries ejected from No.1 scrapper conveyor 1, a part of acetylene gas enters cooler 7, and Pulp pump 5 is by slurry storage tank 1-
Slurry in 1 is transported in reaction kettle 6, and the carbide slag slurries that the conveying of Pulp pump 5 comes enter reaction kettle 6 and start to react, and is generated
Acetylene gas enter cooler 7, carbide slag slurries discharge will be in gas by cooler 7 by the acetylene gas occurred in reaction kettle 6
Condensate moisture, dry acetylene gas enters next process, after dry acetylene gas is pressurizeed by water ring compressor 8
Be transported to later process, the acetylene gas of storage reach be sent to after pressure Acetylene Gas Holder carry out using.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple
The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope should all cover in the scope of the claims of the utility model.
Claims (1)
1. the separator for extracting acetylene gas and tin iron carbon powder in carbide slag slurries occurs for acetylene, it is characterised in that: it includes No.1
Scrapper conveyor (1), slurry storage tank (1-1), No. two scrapper conveyors (2), elevator (3), No. three scrapper conveyors (4), Pulp pump (5), reaction
Kettle (6), cooler (7), water ring compressor (8), acetylene surge tank (9)；The No.1 scrapper conveyor (1) is set to acetylene generator
Bottom, No.1 scrapper conveyor (1) connect with No. two scrapper conveyors (2), and No. two scrapper conveyors (2) are set to the left side of No.1 scrapper conveyor (1)
Lower part, slurry storage tank (1-1) are connect with the right end of No.1 scrapper conveyor (1), and No. two scrapper conveyors (2) connect with elevator (3), are promoted
The upper end of machine (3) is connect with No. three scrapper conveyors (4), and the right end of the slurry storage tank (1-1) is connect with Pulp pump (5), slurry
The gas outlet of storage tank (1-1) is connect with cooler (7), and Pulp pump (5) is connect with reaction kettle (6), reaction kettle (6) and cooler
(7) lower end connection, the upper end of cooler (7) are connect with water ring compressor (8), water ring compressor (8) and acetylene surge tank (9)
Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822099049.3U CN209481574U (en) | 2018-12-11 | 2018-12-11 | The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822099049.3U CN209481574U (en) | 2018-12-11 | 2018-12-11 | The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209481574U true CN209481574U (en) | 2019-10-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822099049.3U Expired - Fee Related CN209481574U (en) | 2018-12-11 | 2018-12-11 | The separator that acetylene gas and tin iron carbon powder are extracted in carbide slag slurries occurs for acetylene |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209481574U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113801695A (en) * | 2021-10-13 | 2021-12-17 | 河南神马氯碱发展有限责任公司 | Device for extracting acetylene gas and tin-iron-carbon powder from acetylene generation carbide slag slurry |
-
2018
- 2018-12-11 CN CN201822099049.3U patent/CN209481574U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113801695A (en) * | 2021-10-13 | 2021-12-17 | 河南神马氯碱发展有限责任公司 | Device for extracting acetylene gas and tin-iron-carbon powder from acetylene generation carbide slag slurry |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191011 |