CN206927636U - A kind of dehydrogenation of isobutane device waste water reclaiming device - Google Patents
A kind of dehydrogenation of isobutane device waste water reclaiming device Download PDFInfo
- Publication number
- CN206927636U CN206927636U CN201720824063.8U CN201720824063U CN206927636U CN 206927636 U CN206927636 U CN 206927636U CN 201720824063 U CN201720824063 U CN 201720824063U CN 206927636 U CN206927636 U CN 206927636U
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- China
- Prior art keywords
- dehydrogenation
- waste water
- water
- isobutane
- molecular sieve
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Abstract
The utility model discloses a kind of dehydrogenation of isobutane device waste water reclaiming device.It includes molecular sieve tank, cooling tower, circulating water pool, the water inlet of the molecular sieve tank is connected by pipeline with the reaction lime set pipeline of dehydrogenation of isobutane device, the delivery port of the molecular sieve tank connects the water inlet of the cooling tower by pipeline, the delivery port of the cooling tower connects the circulating water pool, and circulating water pool connects the circulation of dehydrogenation of isobutane device.The utility model to the caused waste water in dehydrogenation of isobutane device production process by carrying out oil removing, cooling is handled, so that treated waste water has higher water quality, treated waste water is utilized into circulation, the water consumption in production process can be greatly reduced, reduce production cost.It is both environmentally friendly using the utility model processing waste water, by the waste water in production.
Description
Technical field
A kind of dehydrogenation of isobutane device waste water reclaiming device is the utility model is related to, belongs to technical field of chemical.
Background technology
Dehydrogenation of isobutane device needs to inject a large amount of steam in process of production, and steam can finally form reaction lime set, therefore
The waste water of 15 ton hours is produced, not only temperature is higher for caused waste water, and contains oil.Substantial amounts of direct discharging of waste water,
Both not environmentally, substantial amounts of waste is formd again, is unfavorable for reducing production cost.Therefore how effectively to utilize and produced in production process
Raw waste water is a urgent problem to be solved.
Utility model content
For drawbacks described above present in prior art, the utility model, which provides one kind, effectively to be taken off using iso-butane
Hydrogen production device reduces pollution of the waste water to environment in waste water caused by production process, can reduce the dehydrogenation of isobutane of production cost
Device waste water reclaiming device.
The utility model is achieved by the following technical solution：A kind of dehydrogenation of isobutane device waste water reclaiming device,
It is characterized in that：Including molecular sieve tank, cooling tower, circulating water pool, the water inlet of the molecular sieve tank is taken off by pipeline and iso-butane
The reaction lime set pipeline connection of hydrogen production device, the delivery port of the molecular sieve tank connect the water inlet of the cooling tower by pipeline,
The delivery port of the cooling tower connects the circulating water pool, the circulating water of the circulating water pool connection dehydrogenation of isobutane device
System.
Molecular sieve tank in the utility model can be handled the reaction lime set in production process, pass through molecular sieve
Effect fully removes the oil reacted in lime set, and the waste water after molecular sieve tank is handled can be carried out cooling processing by cooling tower,
Water after cooling can enter circulating water pool, be used as recirculated water.Because waste water have passed through oil removing, cooling processing, into circulation
The water quality of the water of water system be improved significantly, not only environmental protection but also strengthen circulating water quality, can greatly reduce in production process
Water consumption.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
In figure, 1, molecular sieve tank, 2, cooling tower, 3, circulating water pool, 4, reaction lime set pipeline.
Embodiment
The utility model is further described below by non-limiting embodiment and with reference to accompanying drawing：
As shown in drawings, a kind of dehydrogenation of isobutane device waste water reclaiming device, it includes molecular sieve tank 1, cooling tower 2, followed
Ring pond 3, the water inlet of the molecular sieve tank 2 is connected by pipeline with the reaction lime set pipeline 4 of dehydrogenation of isobutane device, described
The delivery port of molecular sieve tank 1 connects the water inlet of the cooling tower 2 by pipeline, described in the delivery port connection of the cooling tower 2
Circulating water pool 3, circulating water pool 3 connect the circulation of dehydrogenation of isobutane device.
Molecular sieve tank 1 in the utility model can be handled the reaction lime set in production process, pass through molecular sieve
Effect by react lime set in oil fully remove, cooling tower 2 can be carried out the waste water after molecular sieve tank 1 is handled at cooling
Reason, the water after cooling can enter circulating water pool 3, be used as recirculated water.Because waste water have passed through oil removing, cooling processing, enter
The water quality of the water of circulation be improved significantly, not only environmental protection but also strengthen circulating water quality, can greatly reduce and produce
Water consumption in journey
Other parts in the present embodiment use known technology, will not be repeated here.
Claims (1)
1. a kind of dehydrogenation of isobutane device waste water reclaiming device, it is characterized in that：Including molecular sieve tank (1), cooling tower (2), circulation
Pond (3), the water inlet of the molecular sieve tank (1) are connected by pipeline with the reaction lime set pipeline of dehydrogenation of isobutane device, institute
The delivery port for stating molecular sieve tank (1) connects the water inlet of the cooling tower (2), the delivery port of the cooling tower (2) by pipeline
Connect the circulating water pool (3), the circulation of circulating water pool (3) the connection dehydrogenation of isobutane device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720824063.8U CN206927636U (en) | 2017-07-10 | 2017-07-10 | A kind of dehydrogenation of isobutane device waste water reclaiming device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720824063.8U CN206927636U (en) | 2017-07-10 | 2017-07-10 | A kind of dehydrogenation of isobutane device waste water reclaiming device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206927636U true CN206927636U (en) | 2018-01-26 |
Family
ID=61353778
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720824063.8U Expired - Fee Related CN206927636U (en) | 2017-07-10 | 2017-07-10 | A kind of dehydrogenation of isobutane device waste water reclaiming device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206927636U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109231286A (en) * | 2017-07-10 | 2019-01-18 | 山东海丰能源科技有限公司 | A kind of dehydrogenation of isobutane device waste water reclaiming device |
-
2017
- 2017-07-10 CN CN201720824063.8U patent/CN206927636U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109231286A (en) * | 2017-07-10 | 2019-01-18 | 山东海丰能源科技有限公司 | A kind of dehydrogenation of isobutane device waste water reclaiming device |
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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: 20180126 Termination date: 20200710 |