Device for continuously separating gas hydrate
A gas hydrate and hydrate technology, applied in solid separation devices, gas and liquid fields, can solve the problems of increased investment cost, operation management and maintenance costs, long processing time, poor separation effect, etc. The effect of large processing capacity and easy installation
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2011-07-13
Smart Images
Figure 1 Figure 2 Figure 3
Abstract
Description
technical field
[0001] The invention belongs to the field of gas, liquid and solid separation devices, in particular to a device for continuous separation of other hydrates. Background technique
[0002] At present, using the unique chemical and physical characteristics of hydrates can develop a series of high-tech, involving water resources, environmental protection, climate, oil and gas storage and transportation, petrochemical, biopharmaceutical and many other fields. Typical examples include the hydrate desalination of seawater to make up for the shortage of fresh water resources; the hydrate method permanently reduces the greenhouse gas CO 2 Storage in the seabed to improve the global climate environment; storage, transportation, and distribution of natural gas in the form of hydrate; hydrate separation of low-boiling gas mixtures (such as ethylene cracking gas, various refinery dry gas and natural gas), etc. An important link in the application of these technologies i...
Examples
Embodiment Construction
[0016] Below in conjunction with accompanying drawing and embodiment the present invention will be further described:
[0017] like figure 1 As shown, a device for continuous separation of gas hydrates consists of an upper box and a lower box, the box is connected by an upper flange 20 and a lower flange 21; the upper box is a gas collection chamber 7, and its The top is arched, the upper end is provided with a separation gas outlet 10, a safety valve port 16 and a pressure gauge port 17, and the lower part is provided with a wire mesh demister 6; the lower box is cuboid, and the upper part is provided with a hydrate slurry inlet 1, The cross-section of the hydrate slurry inlet 1 is circular, and the end is provided with a vertical flow equalizer 2. A sieve plate 3 is provided at a distance of 8 to 20 mm from the bottom of the flow equalizer 2. The three sides of the sieve plate 3 are connected to the lower box. The sieve plate 3 is alternately connected with the drainage pla...