| BATCH
PLANT EXPANSION - PHASE I
|
| TIC:
Confidential |
Engineering
Man-hours:
10,000 |
| Client:
Confidential |
Dates:
1994 |
| Location:
Texas
Gulf Coast |
| Scope
of Services:
Preliminary
engineering; P&ID development; capital cost
estimate; detailed engineering and design services;
procurement assistance; pre-commissioning and
start-up assistance.
Project Description:
This
project focused on the addition of the client's
existing facility of a stirred tank reactor
and ancillary systems. The work included:
|
|
|
| • |
A
new process building and structural mezzanine
for new and future reactors and blend facilities. |
| • |
Addition
of reagent storage facilities |
| • |
Addition
of raw materials and finished product storage
tank farm |
| • |
Piperack
and pipebridge additions for new facilities |
| • |
Revise
existing piperacks for piping additions |
| • |
New
Control/MCC building |
| • |
Modifications
to process waste water collection/distribution
systems |
| • |
Upgrade
CWS and CWR systems for increased demands |
| • |
Fire
protection system upgrade |
| • |
Electrical
service and motor control upgrade |
| • |
Process
spill and storm water containment |
| • |
Site
drainage. |
| A
unique issue of this project was increasing
measurement repeatability of batch quantities.
Demar Engineering gave special attention to
piping flexibility and loads imposed by thermal
expansion. The wide range of operating temperature
during the batch cycle created a special challenge
to confirm Code compliance as well as predict
inherent measurement error due to thermal expansion.
The system was modeled with Caesar II software.
Resulting piping and load cell design limited
the error to the tolerance of the load cell
manufacturer.
Engineering,
design and configuration for a plant wide DCS
system was done by Demar's automation group. |
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BATCH
PLANT EXPANSION - PHASE II
|
| TIC:
Confidential
|
Engineering
Man-hours:
8000 |
| Client:
Confidential
|
Dates:
1996/1997 |
| Location:
Texas Gulf Coast |
|
| Scope
of Services:
Preliminary
engineering; P&ID development; capital cost
estimate; detailed engineering and design services;
procurement assistance; pre-commissioning and
start-up assistance.
|
|
|
Project
Description:
This
project was a second expansion to the client's existing
facility over a 5-year period. The process centered on addition
of a new stirred-tank reactor in an existing process building.
During the previous expansion, Demar Engineering anticipated
infrastructure requirements and demands on utilities. With
exception of piperack revisions and mezzanine additions
for the new reactor, most structural and civil demands had
also been addressed in the previous expansion. The new reactor
was installed in an existing process building that had been
designed to accommodate future expansions. New building
structures included bulk catalyst handling and transfer
enclosure and addition to the hot oil heater building. Raw
materials and product storage tanks were added to existing
tank farm storage areas. Again, these facilities had been
designed earlier for expansion flexibility. A new catalyst
system and hot oil system were added for this process.
Engineering,
design and configuration for addition of the new process
to an existing plant wide DCS system was done by Demar Automation.
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RAW
MATERIAL TANK FARM
|
| TIC:
$1,500,000
|
Engineering
Man-hours: 5200 |
| Client:
Pilot Chemical Co.
|
Dates:
2/99 through 5/00
|
| Location:
Houston,
TX
|
|
|
Scope of Services:
Preliminary
engineering; P&ID development; capital cost
appropriation estimate; detailed engineering
and design services; purchasing and construction
management assistance.
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|
|
| Project
Description:
Demar
Engineering provided design services for a plant
raw material tank farm. This storage facility
contains 144,000 gallons of NFPA Class I liquids
in five tanks, 200,000 gallons storage of NFPA
Class II liquids in six tanks and one 230,000
gallon process stormwater storage tank. The
complete facility includes a tertiary HDPE liner,
spill containment, spill segregation and recovery,
transfer pumps, piperacks, new lighting, grounding
and electrical motor control centers.
Product levels and temperatures are monitored
by a Distributed Control System. Discrete high-level
alarm switches offer alarm redundancy and are
part of the spill management plan. Critical
valves and steam heating coils are controlled
by the DCS system.
With exception of the process stormwater storage
tank, all tanks were existing on site and had
to be decommissioned, moved and re-commissioned.
Several of the tanks had to be structurally
upgraded to meet increased operating pressures
imposed by addition of these tanks to the existing
vapor recovery header system. This created special
challenges in coordinating the engineering and
construction work with on-going production schedules.
The work was completed on schedule and below
budget. |
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INSTRUMENTATION
UPGRADE
|
| TIC:
$300,000 |
Engineering
Man-hours: 1000 |
| Client:
Pilot Chemical Co.
|
Dates:
8/99 through 11/99
|
| Location:
Houston, TX
|
|
Scope
of Services:
Preliminary
engineering; P&ID revision; capital cost appropriation
estimate; detailed engineering and design services;
purchasing and construction management assistance; pre-commissioning
and start-up assistance. |
| Project
Description:
Demar
Engineering provided professional services for plant-wide
upgrade of process controls, and emergency shutdown
systems. Work included conversion of pneumatic systems
to electronic, control room revisions, as well as
addition of new field devices for enhanced process
control and process alarms.
The work was completed on schedule and within budget.
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NITRILE
AND AMINE PRODUCTION
|
| TIC:
$3,500,000
|
Engineering
Man-hours: 4500 |
| Client:
Confidential
|
Dates:
11/97 through 5/99
|
| Location:
Dallas, TX Area
|
|
Scope of Services:
Detailed
engineering and design services; purchasing and construction
management assistance |
| Project
Description:
Demar
Engineering provided design and engineering services
for refurbishing and recommissioning existing batch
reactors, storage facilities and process equipment
for nitrile and amine production in an existing chemical
processing plant.
A significant part of the process was a complete redesign
of anhydrous ammonia storage and distribution systems
and addition of an activated catalyst system including
a new catalyst filtering and reclaim building. Demar
Engineering was responsible for building design, specification,
permitting by local authorities, contractor bids,
bid tabulations and purchase requisitions for the
building and related facilities.
|
 |
The
project was particularly challenging due to the client's
desire to re-use existing process controls and mothballed
equipment wherever possible. Since the facilities were spread
across a plant that had evolved over more than 20 years
and involved at least three separate operating units, there
was little standardization. Some of the equipment had been
shut down for several years. Existing motor control centers
(MCC) were modified using parts cannibalized from out-of-service
MCC's in the plant.
The
client performed all process and piping work in-house. During
construction and commissioning our on-site manager assisted
the client with pricing, purchase requisitions and expediting
of bulk materials and process instruments. Much of the work
involved searching the on-site salvage yard for control
valves and pumps that could be re-furbished and incorporated
into the project. Demar Engineering coordinated these efforts.
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MUNICIPAL
UTILITY DISTRICT
|
| TIC:
$3,500,000
|
Engineering
Man-hours: 10,000 |
| Client:
Harris County MUD 366
|
Dates:
1995 to 2000
|
| Location:
Houston, TX
|
|
Scope
of Services:
Construction cost estimate, creation report, bond application,
preliminary and detailed engineering and design; bid
documentation, tabulation; construction documents; construction
inspection |
Project
Description:
In the
mid-eighties the City of Houston annexed an unincorporated
industrial area bordering Northwest Houston. The annexation
of more than 400 acres had a huge tax base but no sanitary
sewerage or potable water systems, other than privately
owned. Demar Engineering has long term relationships with
several of the businesses in this annexed area. Increasing
pressure from the TNRCC on compliance issues led us to explore
the possibility of City-supplied utilities.
Demar
Engineering spearheaded a grass-roots effort to provide
sanitary sewerage and potable water systems for the entire
400-acre site by selling tax-exempt bonds. Demar Engineering
conducted a utility survey to show existing use and to predict
future utility demands and impact. City council members
were contacted along with the appropriate City utility department
directors.
Development
costs were required to perform surveys, preliminary engineering,
provide bond council and cost estimates for a Utility District
Creation Report. We sought out and acquired participation
of three of the largest companies in the proposed district.
The costs were reimbursed when bonds were sold.
Demar
Engineering provided all detailed engineering and construction
inspection. The completed facilities will consist of a 100
thousand gallons per day sewage treatment plant (expandable
to 300 thousand gpd), two lift stations, 15,000 feet of
8-inch and 10-inch sanitary sewer collection lines, and
17,000 feet of 8-inch and 12-inch water main.
By
year end 2000 this project was substantially complete. At
current projections and based on work in place, the project
will be ahead of schedule and within budget.
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BATCH
SPECIALTY CHEMICAL PLANT
|
| TIC:
$1,500,000
|
Engineering
Man-hours: 4500 |
| Client:
Confidential
|
Dates:
1999 through 2000
|
| Location:
Houston, TX
|
|
Scope of Services:
Preliminary
engineering; P&ID development, capital cost estimate;
detailed engineering and design services; purchasing
and pre-commissioning assistance. |
Project
Description:
Demar
Engineering was responsible for design of a fully automated,
state-of-the-art batch specialty chemical plant. Facilities
included:
| • |
Unloading
and storage of raw materials and reagents |
| • |
Reaction
with reagents including corrosives and aromatic hydrocarbons |
| • |
Neutralization
and evaporative concentration of the finished product |
| • |
Product
storage and loadout. |
Because
of corrosive process conditions, construction materials
included stainless steel and glass-lined equipment and piping
as well as graphite heat exchangers.
Demar
Engineering also modified the plant's existing utility distribution
and wastewater collection systems, integrated a state-of-the-art
process automation system for the new unit with the plant's
existing computer control system, reviewed local building
code requirements, and submitted necessary permit applications.
The
process area piping was designed using 3-dimensional modeling
techniques (AutoCAD 2000 and CADWorx/PIPE).
Engineering
and design services were completed on schedule and within
budget.
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