Site condition and design: Difference between revisions

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== References ==
== References ==
* Gavin Towler and Ray Sinnott, Chapter 11 - General Site Considerations, In Chemical Engineering Design (Second Edition), edited by Gavin Towler and Ray Sinnott, Butterworth-Heinemann, Boston, 2013, Pages 505-524, ISBN 9780080966595, http://dx.doi.org/10.1016/B978-0-08-096659-5.00011-0.
* Gavin Towler and Ray Sinnott, Chapter 11 - General Site Considerations, ''Chemical Engineering Design'', edited by Gavin Towler and Ray Sinnott, Butterworth-Heinemann, Boston, 2013, Pages 505-524, ISBN 9780080966595, http://dx.doi.org/10.1016/B978-0-08-096659-5.00011-0.
(http://www.sciencedirect.com/science/article/pii/B9780080966595000110)
(http://www.sciencedirect.com/science/article/pii/B9780080966595000110)

* M.S. Peters, K.D. Timmerhaus, ''Plant Design and Economics for Chemical Engineers'', 5th Ed., McGraw-Hill: New York, 2003.

* J.C. Mchkelnburgh, ''Plant Design and Economics for Chemical Engineers'', Halsted Press: New York, 1985.


== External links==
== External links==

Revision as of 16:13, 18 January 2014

Title: Site condition and design

Authors: Alex Chandel, Eric Jiang, Minwook Kim, Todor Kukushliev, William Lassman

Stewards: Alex Chandel, Eric Jiang, Minwook Kim, Todor Kukushliev, William Lassman

Date Revised: 1/17/2014

Introduction

All chemical processes require land for chemical storage, process equipment, and labor facilities.

Geographical selection

The location surrounding a chemical plant can substantially influence its construction costs and operating costs, and may affect long-term profitability. Thus it is important to choose an appropriate location for every facility.

Factors considered

Natural resources

Proximity to continental and underwater oil deposits, natural gas, coal mines, and other resources.

Weather

Its influence on ambient temperature and thus on utility cost.[ citation needed ] Also rain and humidity, and the sensitivity of the process to water exposure.

Proximity to related chemical operations

Oil rigs are found in the gulf, and oil refineries on its shore. Biofuel production plants are found in the midwest.[ citation needed ]

Laws and regulations

Some states are more friendly to chemical engineering operations, or may impose additional regulations. Property costs, property taxes, corporate income taxes, and environmental contamination fines will vary between states.

Waste Minimization and Management

Waste Minimization

Production of waste is arises naturally in any plant and require a noticeable amount of resources to take care of. Before even considering methods of managing ways, cost can significantly be reduced by efficient management by source reduction. Below are some source reduction strategies which can be employed:

1. Purification of feeds.

2. Protect catalysis and adsorbents.

3. Eliminate use of extraneous materials.

4. Increase recovery from separations.

5. Improve fuel quality.

Headline text

Waste Management

Cost

All of the above criteria ultimately influence the capital and operating costs of a plant, and its expected lifespan.

Local wages, prices of chemical feedstock, shipping costs, and utilities all contribute to total operating costs.

Property prices, rental fees, taxes, and existing company property in the area contribute to recurring investment costs.

Common locations

There are many common locations for chemical processes, often specific to one or more industries.

The Gulf of Mexico

Texas - petrochemical refineries

Louisiana

Alaska

(China)

(Arabian peninsula)

etc

Site Design and Construction

Site Layout

The needs of a site for a chemical process vary considerably from process to process. In general, however, all chemical plants require the following:

  • Shipping and receiving of products and raw materials
  • Storage
  • Utilities
  • Offices and laboratories for management and quality control personnel
  • Medical and fire services for emergency management
  • Cafeterias, parking lots, and other amenities for employees.

(All this came from Towler/Sinnot page 508-510)

These auxiliary buildings are often referred to as ancillary structures and they are placed within a chemical process to minimize transportation of goods and personnel, and to maximize safety. The following procedure is followed when determining the site layout of a chemical process:

1. Major process equipment is placed in a logical order to minimize transportation of process streams. Extra emphasis is placed on the separation and treatment of hazardous materials as quickly as possible.
2. Utilities such as boilers and power plants are placed to minimize transportation of utility to its use within the process. Utilities are usually consolidated into one section of the chemical plant because they are usually generated together. For example, a boiler produces high pressure steam; half the steam is sent through a turbine to generate electricity and to expand the steam into low pressure steam.
3. Shipping and receiving are placed wherever there is a need to conform to preexisting infrastructure. For example, if the plant is located on a harbor, shipping and receiving for all barge shipments are located by the water. If the plant is built next to a railway, shipping by rail is located next to the tracks.
4. Storage tanks and warehouses are consolidated as much as possible. Storage of raw materials and products are stored between where they enter or exit the process and where they are shipped or received.
5. Ancillary buildings are placed to minimize time personnel spend traveling around the site.
6. Offices and labs are located as far away from hazardous processes as possible.
7. Walkways and roadways are added as needed to assist with construction and transportation during plant operation.

(All this came from Mecklenburgh, J. C. (Ed.). (1985). Process plant layout. Godwin/Longmans.)

Site Construction

(All information came from Mecklenburgh, J. C. (Ed.). (1985). Process plant layout. Godwin/Longmans for this section). Site construction, along with process design, is an iterative process that follows a multi-step procedure.

Stage One Layout

The "Proposal" or Stage One layout is the first step towards designing a site layout. The purpose of the Stage One layout is to assess the feasibility of the process according to the cost, hazard, risk, and environmental standards set by the interested parties.

The information included in a Stage One layout is the relative position of buildings and process equipment, and any other data that may come from a preliminary case study of a particular process. Additionally, preliminary estimates by manufacturers and contractors for process equipment and ancillary structures, as well as local building codes and regulations are used in generating the Stage One Layout.

Usually, different layouts for the same process may produce different costs. At this stage in development, many different layouts should be generated and the different layouts should be compared in a systematic way. It is usually very difficult to tell which layout is superior based purely on inspection. Once a Stage One design is finalized, the layout can move on to the next stage.

Stage Two Layout

Stage Two Layouts are generated based on the finalized Stage One design. Changes to the Stage One design are minimized. The purpose of the Stage Two Layout is to determine an accurate detailed cost of the entire process. Additionally, detailed hazard and environmental information is determined and submitted to all involved regulatory parties at this stage.

Final Stage Layout

After the detailed cost information, hazard, and environmental information are approved, the Final Design layout commences. At this stage, detailed drawings of all equipment, piping, and layouts are finalized. At the conclusion of the Final Stage layout, orders with contractors are placed and fabrication of process equipment begins, and the site land is purchased. Essentially, this is the "point of no return."

Construction

The first step in constructing the plant is remediation and preparation of the land for construction of a chemical plant. This can include clearing the land of trees and vegetation, removing other natural obstacles such as boulders and ditches, implementing a drainage system, landscaping, grading to remove difficult topography, and anything else that is necessary. Site selection attempts to minimize costs associated with this step, but there is invariably some form of preparation required for every site.

The second step is to construct all roadways, sidewalks, and fences required for both plant operation and plant construction. Costs associated with this step can range from 2 to 10 percent of the total capital investment for a chemical plant (CITE SOURCE 5, PAGE 246).

Process equipment and buildings are then constructed as soon as they are available. While construction schedules vary considerably from process to process, in some cases it is possible to perform the final construction steps once the process has already begun to operate, and the construction schedule is designed with this in mind (CITE Mecklenburgh, J. C. (Ed.). (1985). Process plant layout. Godwin/Longmans.).

A new aspect of construction of process equipment is a modular approach, where process equipment is assembled as completely as possible by the manufacturer and shipped while assembled. The advantage to this approach is a more comprehensive testing of the equipment by the manufacturer and less installation time once the equipment has arrived on site (Towler page 510-511).

Footprint

Areas with greater land costs require vertically oriented equipment.[ citation needed ]

References

  • Gavin Towler and Ray Sinnott, Chapter 11 - General Site Considerations, Chemical Engineering Design, edited by Gavin Towler and Ray Sinnott, Butterworth-Heinemann, Boston, 2013, Pages 505-524, ISBN 9780080966595, http://dx.doi.org/10.1016/B978-0-08-096659-5.00011-0.

(http://www.sciencedirect.com/science/article/pii/B9780080966595000110)

  • M.S. Peters, K.D. Timmerhaus, Plant Design and Economics for Chemical Engineers, 5th Ed., McGraw-Hill: New York, 2003.
  • J.C. Mchkelnburgh, Plant Design and Economics for Chemical Engineers, Halsted Press: New York, 1985.

External links

  • (Relevant wikipedia article)